Journal Pre-proof Boosting the Electrochemical Performance of 3D Composite Lithium Metal Anodes through Synergistic Structure and Interface Engineering Yuanmao Chen, Xi Ke, Yifeng Cheng, Mouping Fan, Wenli Wu, Xinyue Huang, Yaohua Liang, Yicheng Zhong, Zhimin Ao, Yanqing Lai, Guoxiu Wang, Zhicong Shi PII:
S2405-8297(19)31101-8
DOI:
https://doi.org/10.1016/j.ensm.2019.12.023
Reference:
ENSM 1029
To appear in:
Energy Storage Materials
Received Date: 27 September 2019 Revised Date:
8 December 2019
Accepted Date: 12 December 2019
Please cite this article as: Y. Chen, X. Ke, Y. Cheng, M. Fan, W. Wu, X. Huang, Y. Liang, Y. Zhong, Z. Ao, Y. Lai, G. Wang, Z. Shi, Boosting the Electrochemical Performance of 3D Composite Lithium Metal Anodes through Synergistic Structure and Interface Engineering, Energy Storage Materials, https:// doi.org/10.1016/j.ensm.2019.12.023. This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing this version to give early visibility of the article. Please note that, during the production process, errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain. © 2019 Published by Elsevier B.V.
Boosting the Electrochemical Performance of 3D Composite Lithium Metal Anodes through Synergistic Structure and Interface Engineering Yuanmao Chen1,2, Xi Ke1,2,*, Yifeng Cheng1,2, Mouping Fan1,2, Wenli Wu1,2, Xinyue Huang1,2, Yaohua Liang1,2, Yicheng Zhong1,2, Zhimin Ao3, Yanqing Lai4, Guoxiu Wang5,* and Zhicong Shi1,2,* 1
Smart Energy Research Centre, School of Materials and Energy, Guangdong University of Technology, Guangzhou 510006, China 2
Guangdong Engineering Technology Research Center for New Energy Materials and Devices, Guangzhou 510006, China 3
Guangzhou Key Laboratory of Environmental Catalysis and Pollution Control, Institute of Environmental Health and Pollution Control, School of Environmental Science and Engineering, Guangdong University of Technology, Guangzhou 510006, China
4
School of Metallurgy and Environment, Central South University, Changsha, 410083, China
5
Centre for Clean Energy Technology, School of Mathematical and Physical Sciences, University of Technology Sydney, Sydney NSW 2007, Australia * Corresponding author: E-mail:
[email protected] (X. Ke),
[email protected] (G. Wang),
[email protected] (Z. Shi)
Author Contribution Statement Yuanmao Chen: Conceptualization, Investigation, Validation, Data curation, Writing-Original
draft
preparation.
Xi
Ke:
Supervision,
Conceptualization,
Methodology, Data Curation, Writing-Reviewing and Editing. Yifeng Cheng: Investigation. Mouping Fan: Investigation. Wenli Wu: Data curation. Xinyue Huang: Data curation. Yaohua Liang: Visualization. Yicheng Zhong: Visualization. Zhimin Ao: Software. Yanqing Lai: Validation. Guoxiu Wang: Writing-Review and Editing. Zhicong Shi: Conceptualization, Validation, Supervision.
1
Boosting the Electrochemical Performance of 3D Composite
2
Lithium Metal Anodes through Synergistic Structure and
3
Interface Engineering
4 5
Abstract: Construction of three-dimensional (3D) composite lithium metal anodes (LMAs)
6
based on Li melt-infusion into a 3D porous scaffold has been demonstrated to be effective for
7
solving the issue of the considerable relative volume change of LMAs during Li
8
plating/stripping. However, little attention has been paid to controllable regulation of the
9
structure and interface of 3D composite LMAs. In this study, 3D composite LMAs, namely
10
Li-AuLi3@CF electrodes, are firstly fabricated by infusion of molten Li into carbon fiber (CF)
11
paper modified with nanoporous gold (NPG) which is converted to AuLi3 after infusion. We
12
herein demonstrate a synergistic structure and interface engineering strategy realized by a
13
simple and effective pre-stripping protocol to initially expose a portion of the 3D AuLi3@CF
14
scaffold to create “PS-Li-AuLi3@CF” electrodes, which greatly boosted the electrochemical
15
performance. Symmetrical Li|Li cells with PS-Li-AuLi3@CF electrodes show an overpotential
16
of 111 mV after cycling at a current density of 0.5 mA cm-2 for 1800 h. Additionally, Li|LiFePO4
17
(LFP) and Li|sulfurized polyacrylonitrile (SPAN) full cells with PS-Li-AuLi3@CF electrodes
18
exhibit a high capacity retention of 96.1% with a Coulombic efficiency (CE) of 99.2% after
19
1000 cycles at 5C, and a capacity retention of 70.6% with a CE of 99.8% after 1000 cycles at 2C,
20
respectively. This work provides a simple and highly effective method for engineering the
21
structure and interface of 3D composite LMAs to boost their electrochemical performance for
22
high-energy-density rechargeable lithium metal batteries (LMBs). 1
23
Keywords: lithium metal anodes, pre-stripping, structure engineering, interface engineering,
24
nanoporous gold
25 26
1. Introduction
27
Traditional lithium ion batteries (LIBs) based on reversible intercalation/decalation of lithium
28
ions are approaching their energy density limits and not meeting the ever-increasing demand of
29
today’s electric power and energy storage applications including electric vehicles and portable
30
devices[1-3]. In pursuing next-generation batteries with significantly higher energy density,
31
alternative systems beyond lithium intercalation chemistry have been developed such as
32
Li-S[4] and Li-O2[5, 6] systems based on Li metal plating/stripping electrochemistry. In these
33
systems, Li metal, which possesses fascinating advantages of an ultrahigh specific capacity
34
(3860 mAh g-1), a very low redox potential (-3.040 V versus standard hydrogen electrode) and a
35
small gravimetric density (0.534 g cm-3), has been widely considered to be the ultimate anode
36
material to replace graphite anodes[7-10]. However, practical usage of lithium metal anodes
37
(LMAs) has been challenged by the issues of low Coulombic efficiency (CE) and Li dendrite
38
growth, originating from the highly reactive nature of Li metal in organic electrolyte and an
39
unstable solid electrolyte interphase (SEI), as well as nontrivial volume change during Li metal
40
plating/stripping[11-13]. In order to solve these problems, a large number of strategies, for
41
example, adding electrolyte additives to facilitate SEI formation[14, 15], constructing artificial
42
SEI films to protect LMAs from electrolyte attack[16-19], modifying separators to homogenize
43
Li ion flux[20, 21], improving lithiophilicity to reduce lithium nucleation overpotential[22-26],
44
have been developed and effectively prolonged the lifespan of LMAs. However, these 2
45
strategies are usually effective at relatively low current densities and cycling capacities, and
46
need further improvements for high-rate battery applications. Structure-engineered composite
47
electrodes with embedded hosts which can stabilize Li plating/stripping process are demanded
48
for high-rate, high-capacity and long-lifespan LMAs[27-33].
49
Three-dimensional (3D), highly porous current collectors and skeletons have been
50
introduced into LMAs as 3D hosts to improve electrochemical performance. These 3D hosts
51
can effectively suppress lithium dendrite growth not only by accommodating huge volumetric
52
change but also by reducing the effective current density during Li plating/stripping
53
processes[12, 34]. However, most of these structured LMAs are initially Li-free, and require
54
pairing with Li-containing cathodes, which results in a lack of Li to offset irreversible
55
consumption of lithium during SEI formation and later cycling. In order to match Li availability
56
at both ends of the cell when including Li-free cathodes, such as in high-energy-density S and
57
O2 cathodes, electrochemical plating of lithium into these 3D hosts prior to cell assembly is
58
necessary[35, 36], which usually causes uneven Li deposition, and also makes this process
59
infeasible for battery manufacturing industry. Therefore, pre-storing of Li metal into 3D hosts is
60
important for obtaining a composite lithium metal electrode. In this regard, Cui et al. are
61
pioneers. They developed a facile and effective method to fabricate composite LMAs by
62
infiltrating molten Li metal into 3D hosts[29]. Using this method, a variety of 3D highly porous
63
scaffolds, such
64
wood/polymer[28], have been employed to produce 3D composite LMAs. Compared with
65
hostless Li metal electrodes, such 3D composite LMAs are capable of confining Li metal within
66
3D matrices, and maintaining a relatively constant electrode dimension, thus addressing the
as nickel foam[37], carbon cloth/paper[30, 38] and carbonized
3
67
issue of large volume change associated with Li plating/striping, and realizing dendrite
68
suppression and stable cycling. Nevertheless, most of reported 3D hosts have lithiophobic
69
surfaces that need lithiophilicity conversion, and therefore, an extra phase, such as ZnO[39, 40],
70
SnO2[41] and Si[29], have frequently been introduced to enhance lithiophilicity. The
71
modification process always demands complicated facilities, e.g., chemical vapor deposition
72
and atomic layer deposition, which are often labour-intensive, time-consuming and highly
73
expensive. More importantly, such semiconducting phases lower electronic conductivity at the
74
host-Li interface, which was usually overlooked in previous studies. In this manner,
75
development of novel and simple strategies for constructing a lithiophilic and highly
76
conductive interface on 3D hosts is of tremendous importance for fabricating 3D composite
77
LMAs. In addition to a lithiophilic interface, the electrode structure of 3D composite LMAs is
78
another important factor that contributes significantly to overall performance. However, it is a
79
great challenge to control the electrode structure of 3D composite LMAs during the fabrication
80
procedure, since the infusion process of molten Li metal is completed in a spontaneous manner
81
within a short time period. Thus, in order to boost the electrochemical performance of 3D
82
composite LMAs, there is a need for an alternative way to regulate the electrode structure after
83
the melt-infusion process. So far, very little attention has been paid to the pretreatment of 3D
84
composite LMAs.
85
In this study, we propose a synergistic structure and interface engineering strategy, which is
86
simple and easy to conduct without the use of complicated instruments, to construct a newly
87
designed 3D composite LMA for boosting its electrochemical performance. Specifically, a
88
lithiophilic nanoporous gold (NPG) film with hierarchical micro/nano-porosity was initially 4
89
coated on the surface of carbon fibers (CF), which reacts with molten Li and converts to a
90
AuLi3 film during molten Li infusion process. Due to the fact that the AuLi3@CF scaffold was
91
completely buried in Li metal layer after the melt-infusion process, a fraction of Li metal was
92
then stripped from the 3D composite LMA (Li-AuLi3@CF) in order to expose the upper porous
93
AuLi3@CF structure. We term this treatment process as “pre-stripping” (PS) of 3D composite
94
LMAs. The as-designed 3D composite LMA (PS-Li-AuLi3@CF) possesses some remarkable
95
advantages: (i) the pre-stripped AuLi3@CF scaffold is highly porous and conductive, which
96
promotes rapid and homogeneous electron/ion transport at the PS-Li-AuLi3@CF/electrolyte
97
interface, allowing fast electrode kinetics; (ii) the surface of the pre-stripped scaffold, namely
98
the AuLi3 phase, is highly lithiophilic, which can bring about a much lower Li nucleation
99
overpotential, enabling suppression of Li dendrite growth; (iii) the pre-stripped scaffold has a
100
relatively large surface area, which can significantly reduce local current densities during
101
cycling, thus enlarging the Sand’s time[42] and retarding Li dendrite formation; (iv) the
102
released void space of pre-stripped scaffold provides extra room to accommodate Li deposition,
103
alleviating the huge volume change during Li plating/stripping. Owing to the above mentioned
104
merits, the PS-Li-AuLi3@CF based 3D composite LMAs exhibit outstanding electrochemical
105
performance. In Li|Li symmetric cells, PS-Li-AuLi3@CF based 3D composite LMAs can run
106
for 1800 h without cell failure at a current density of 0.5 mA cm-2. PS-Li-AuLi3@CF|LiFePO4
107
(LFP) cells show an excellent capacity retention of 96.1% with a CE of 99.2% after 1000 cycles
108
at 5C. Furthermore, PS-Li-AuLi3@CF|sulfur/polyacrylonitrile (SPAN) cells deliver a capacity
109
retention of 70.6% with a high CE of 99.8% after 1000 cycles at 2C.
110 5
111
2. Experimental Section
112
2.1. Fabrication of NPG@CF scaffolds
113
The fabrication procedure of NPG@CF scaffolds consists of two steps. Firstly, a
114
commercial CF (Toray Carbon Fiber Paper, Japan) paper was cut into rectangular pieces with
115
a size of 1×6 cm2 and successively washed with acetone, dilute hydrochloric acid solution,
116
ethanol, and distilled water in an ultrasonic bath for 20 min to remove impurities on the CF
117
surface, and then dried in a vacuum oven at 60 °C. The AuSn alloy film was electrodeposited
118
onto the pre-treated CF with an area of 1 cm2 exposed in the electrolyte at a current density of
119
5 mA cm-2 for 20 min at 45 °C, using the CF and the Pt-modified Ti mesh as the working and
120
counter electrodes, respectively. Secondly, the AuSn alloy modified CF (AuSn@CF) scaffolds
121
were immersed into a solution containing 5 mol L-1 NaOH and 1 mol L-1 H2O2 for one week
122
at room temperature for fully dealloying the Sn component to obtain NPG@CF scaffolds.
123 124
2.2. Fabrication of PS-Li-AuLi3@CF electrodes
125
PS-Li-AuLi3@CF electrodes were fabricated based on a combination of Li melt-infusion
126
into NPG@CF scaffolds and pre-stripping of Li metal. The whole fabrication procedure was
127
accomplished in an argon-filled glove box with an oxygen and water level below 0.1 ppm.
128
Firstly, both sides of Li foils were scratched and polished with a sharp scalpel until the
129
surfaces were exceedingly shiny, then the polished Li foils were put onto a heating station
130
padded with a piece of Ni foil at 400 °C. NPG@CF scaffolds were laid on the molten Li
131
surface to absorb molten Li. Secondly, Li-AuLi3@CF electrodes were assembled in CR2032
132
coin cells with Li foils as the counter/reference electrodes, and a specific amount of Li metal 6
133
was stripped from Li-AuLi3@CF electrodes to obtain PS-Li-AuLi3@CF electrodes. For
134
comparison, pristine CF scaffolds were also put on molten Li surface to absorb molten Li into
135
the bottom part of scaffolds to obtain Li@CF composite electrodes (Fig. S1).
136 137
2.3. Computational details
138
Calculations were performed using density functional theory (DFT) as implemented in the
139
Vienna ab initio simulation package (VASP)[43]. The interaction between ions and electrons
140
is described using ultrasoft pseudopotentials[44]. The generalized gradient approximation
141
(GGA)
142
exchange-correlation functional[45]. The cell structure was fully optimized using the
143
Broyden-Fletcher-Goldfarb-Shanno (BFGS) minimization technique[46]. The cut-off energy
144
of the plane wave was set to 400 eV, and the Brillouin zone sampling was performed using a
145
7×7×1 set of the Monkhorst–Pack mesh for the slab model of AuLi3(111) and graphite(0001).
146
The convergence thresholds of geometry optimization were set to be 1×10-6 eV/atom for the
147
energy change and 0.015 eV/Å for the maximum force. The optimization would stop when
148
these criteria were satisfied. Adsorption energies Eads of Li atom on the surface of AuLi3(111)
149
and graphite(0001) was calculated as follows:
with
the
Perdew-Burke-Ernzerhof
(PBE)
functional
was
used
as
the
150
Eads = Etotal – Eslab – ELi
151
where Etotal and Eslab are the total energies of the relaxed slab model with and without Li atom,
152
respectively, and ELi is the energy of isolated Li atom.
153 154
2.4. Characterization 7
155
X-ray diffraction (XRD, Rigaku D/max-2200/PC) using a Cu Kα radiation source at a
156
wavelength of 0.1541 nm was conducted to confirm the crystal structures of scaffolds and
157
composite Li metal electrodes. Brunauer-Emmett-Teller (BET) surface area measurements of
158
electrodes were carried out using a specific surface analyzer (SSA, BeiShiDe, 3H-2000).
159
Field-emission scanning electron microscopy (FESEM, JEOL, JSM-6700F) was employed to
160
characterize surface morphology of electrodes. Specifically, before characterization, coin cells
161
were firstly disassembled in a glovebox to obtain electrodes, which were immersed into
162
1,3-dioxolane/dimethoxyethane (DOL/DME) solvents to remove residual electrolyte and Li
163
salt, and then dried for minutes. An anaerobic sealed box was used to transfer the samples
164
from the glovebox to the SEM chamber.
165 166
2.5. Electrochemical measurements
167
CR2032-type symmetrical Li|Li coin cells with two identical Li foil, Li-AuLi3@CF and
168
PS-Li-AuLi3@CF electrodes, respectively, were assembled in an argon-filled glovebox with a
169
Celgard separator and an electrolyte of 1 M LiPF6 in EC/DEC (1:1 vol%) without any
170
additives. The amount of electrolyte used in assembling a cell was about 25 µL. The Li|Li
171
cells were galvanostatically cycled at current densities of 0.5, 1 and 3 mA cm-2 with a capacity
172
of 1 mAh cm-2 using LAND battery testing system at room temperature. Full cells were
173
assembled with Li foil, Li-AuLi3@CF and PS-Li-AuLi3@CF electrodes as the anodes, and
174
LiFePO4 (LFP) with an areal loading of 2.15 mg cm-2 and sulfurized polyacrylonitrile (SPAN)
175
with an areal S loading of 0.49 mg cm-2 as the cathodes, respectively, employing the same
176
separator and electrolyte as those in Li|Li cells. For full-cell cycling, the cells were firstly 8
177
cycled at 0.2 C for 2 cycles for cell activation and SEI formation, and Li|LFP and Li|SPAN
178
cells were cycled in voltage windows of 2.4-4.2 V and 1.0-3.0 V (vs Li+/Li), respectively.
179
Electrochemical impedance spectra (EIS) measurements were conducted using an
180
electrochemical workstation (ZIVE, SP1) over a frequency range from 100 kHz to 10 mHz.
181 182
3. Results and discussion
183
Fig. 1a illustrates the fabrication process of PS-Li-AuLi3@CF electrodes. CF paper was
184
chosen in this study as a 3D host due to its lightweight as well as high electrical conductivity
185
and porosity. However, the pristine CF surface is intrinsically lithiophobic, which makes it
186
difficult to spontaneously wet with molten Li metal. Therefore, in order to enhance the surface
187
lithiophilicity of CF paper, we firstly adopted a facile method developed previously in our
188
group to coat a nanoporous gold (NPG) film on the CF skeleton, which was accomplished by a
189
combination of AuSn alloy electrodeposition and chemical dealloying of Sn[47]. It is worth
190
noting that NPG, rather than gold nanoparticles[22, 25] used in previous studies, was employed
191
as the lithiophilic phase herein because the 3D hierarchical micro- and nanoporosity of the NPG
192
film could bring multiple advantages. Details will be published elsewhere. Then, the NPG@CF
193
scaffold was put into contact with molten Li metal. NPG reacted with molten Li to form AuLi3
194
and a significant quantity of molten Li metal was infused into the scaffold, giving a fully
195
Li-infused CF electrode (Li-AuLi3@CF). Finally, a portion of Li metal was stripped via a
196
pre-stripping treatment of the Li-AuLi3@CF electrode (PS-Li-AuLi3@CF), to expose the top
197
part of the AuLi3@CF scaffold. Fig. S2 displays optical images of a CF-based electrode at
198
different fabrication stages. The color appearance of the CF electrode turns sequentially from 9
199 200
Figure 1. Schematic illustration (a) and SEM images under different magnifications of pristine
201
CF (b, g), AuSn alloy coated CF (AuSn@CF) (c, h), NPG coated CF (NPG@CF) (d, i),
202
NPG@CF after molten Li infusion (Li-AuLi3@CF) (e, j), and Li-AuLi3@CF after pre-stripping
203
(PS-Li-AuLi3@CF) (f, k).
204 205
gray-black to grey, gold, silvery, and then yellow-white after AuSn alloy electrodeposition,
206
chemical dealloying of Sn, melt-infusion of Li metal, and pre-stripping of Li metal, respectively.
207
The color change of the electrode is very uniform, which indicates the structure and surface of
208
the electrode have been homogeneously modified by this protocol, which was confirmed by 10
209
scanning electron microscopy (SEM) as shown in Fig. 1b-k. The pristine CF paper electrode
210
shows a highly porous 3D structure (Fig. 1b) consisting of an interconnected network of smooth
211
fibers with a diameter of about 8 µm (Fig. 1g). After electrodeposition of AuSn alloy, the AuSn
212
alloy film was conformally wrapped on fiber surfaces (Fig. 1c). The higher magnification SEM
213
images (Fig. 1h and Fig. S3a) reveal that the alloy film was composed of densely stacked
214
microscale polygonal bricks with a thickness of 150~200 nm. After chemical dealloying of Sn
215
component, the scaffold displays a uniformly rough and porous surface (Fig. 1d). In line with
216
our previous study[47], the dealloying process transforms the solid AuSn bricks into
217
bicontinuous porous NPG sheets (Fig. 1i and Fig. S3b), as confirmed by XRD result shown in
218
Fig. S4a. Meanwhile, energy dispersive spectroscopy (EDS) mapping results reveal that C, Au
219
and Sn components in AuSn@CF, and C, Au components in NPG@CF samples are uniformly
220
distributed (Fig. S5). Such a lithiophilic NPG film with hierarchical porosity (microscale
221
porosity among NPG sheets and nanoscale porosity inside NPG sheets) can not only provide a
222
large chemical driving force through Au-Li alloy reaction, but also form a considerable
223
physical drawing force by capillary absorption. Besides these effects, this hierarchical
224
micro/nano-porosity could also help to anchor the deposited Li metal, thus significantly
225
improving the stability of CF-Li interface. As a result, the NPG@CF electrode exhibits a very
226
fast uptake of molten Li metal (Fig. S6a and Movie S1), while the pristine CF electrode is
227
relatively difficult to fully wet by molten Li (Fig. S6b and Movie S2). Owing to superior
228
lithiophilicity of NPG@CF electrodes, it is noted that molten Li was fully infused into
229
electrodes within two seconds and thus it is not convenient to control the amount of infused
230
molten Li during such a short period, which is different to previous studies where infusion 11
231
processes can take as long as tens of seconds[48-50]. After melt-infusion of Li metal, the
232
composite electrode displays a compact structure with the CF scaffold fully embedded in Li
233
metal (Fig. 1e, j and Fig. S7a). Meanwhile, XRD results reveal that gold phase was converted to
234
AuLi3 phase as shown in Fig. S4b. It can be inferred that, when paired with a Li-containing
235
cathode, such a fully-infused composite LMA would behave like a hostless Li electrode owing
236
to the ineffectiveness of buried AuLi3@CF scaffold. When matched with a Li-free cathode, the
237
first discharge process unmasks the outermost extent of the AuLi3@CF scaffold, but the effect
238
of the AuLi3@CF scaffold could be significantly attenuated during the Li stripping process
239
(especially during the initial period of the discharge), since the exposure of the AuLi3@CF
240
scaffold takes place gradually throughout the discharge process. In this context, it is reasonable
241
to conduct a pre-stripping process to pre-expose the 3D AuLi3@CF scaffold to fully activate its
242
multifunctional capabilities as mentioned above. Moreover, removal of excessive Li metal will
243
achieve a higher energy density for a cell. After 10 mAh cm-2 of Li metal is stripped out, the
244
PS-Li-AuLi3@CF electrode displays a highly porous structure with unformly stripped fibers
245
(Fig. 1f and Fig. S7b). A higher magnification SEM image (Fig. 1k) shows that the fiber surface
246
exhibits a different morphology compared with the initial stage as shown in Fig. 1i, and XRD
247
results reveal that the surface layer is composed mainly of AuLi3 phase (Fig. S4c). It should be
248
noted that although a high surface area of 3D current collectors can reduce the effective current
249
density during Li plating/stripping process and retard Li dendrite growth[12, 34], it may also
250
lead to additional side reactions and severe SEI formation. The BET measurement shows that
251
the surface area of PS-Li-AuLi3@CF electrodes is about 2.3 m2 g-1. This value is relatively
252
small compared with that of other previously reported 3D scaffolds with a stable SEI layer 12
253
during cycling[51, 52]. Hence, the exposed surface area of PS-Li-AuLi3@CF electrodes would
254
not cause severe SEI formation.
255 256
Figure 2. Calculated binding energies of a Li atom on a AuLi3 slab with (a) a Au-terminated
257
surface or (b) a Li-terminated surface, and (c) a pristine CF slab for comparison. (d) Voltage
258
profiles of galvanostatic Li deposition on a PS-Li-AuLi3@CF and a pristine CF electrodes at a
259
current density of 0.5 mA cm-2 with the inset showing comparison of Li nucleation
260
overpotentials on the two electrodes.
261 262
As reported in our previous study, the AuLi3 phase was found to be effective in suppressing
263
the growth of Li dendrites and prolonging the lifespan of LMAs[25]. Herein, we further
264
employed density functional theory (DFT)[53] to investigate the origin of this effect by
265
calculating the binding energies between a Li atom and the AuLi3 or the carbon fibre (Fig. 2a-c). 13
266
It should be noted here that the structural model of the AuLi3 alloy slab presents two different
267
cleaved surfaces, namely the Au-terminated and the Li-terminated surfaces, respectively. The
268
theoretical calculations reveal that both the Au-terminated and the Li-terminated AuLi3(111)
269
surfaces exhibit much larger binding energies of -2.29 and -1.81 eV, respectively, compared
270
with -1.42 eV for the pristine CF, indicating that the coated AuLi3 phase is much more
271
lithiophilic than the pristine CF surface. As has been well demonstrated by previous
272
studies[22-26], a lithiophilic modification of the host surface is capable of reducing nucleation
273
overpotential of Li metal and guiding uniform Li plating/stripping, thus enabling suppression of
274
Li dendrite growth and prolonging the lifespan of LMAs. Herein, thanks to the excellent
275
lithiophilicity of the AuLi3 layer, the nucleation overpotential of Li metal on the
276
PS-Li-AuLi3@CF electrode (30 mV) was much smaller than that on the pristine CF electrode
277
(55.8 mV) (Fig. 2d). Compared with previous studies using discretely distributed metallic
278
nanoparticles[22, 50] or semiconductive thin films[29, 39] as lithiophilic species, the
279
continuous AuLi3 film with superior electrical conductivity employed in the present study
280
could not only provide homogeneously dispersed lithiophilic sites on the host surface, but also
281
supply a highly conductive and continuous interface between the host and the Li metal. Owing
282
to these characteristics, the PS-Li-AuLi3@CF electrode is reasonably expected to exhibit stable
283
Li plating/stripping behavior and excellent electrochemical performance in lithium metal
284
batteries (LMBs).
285
In order to reveal the effect of AuLi3 film on Li plating/stripping behavior, CR2032-type coin
286
cells were assembled with PS-Li-AuLi3@CF and Li@CF (see Experimental Section for details)
287
electrodes as the working electrode, and a Li foil as the counter electrode. An amount of 5 mAh 14
288 289
Figure 3. Representative voltage-time profiles of a galvanostatic Li plating/stripping cycle at a
290
current density of 0.5 mA cm-2 with a plating/stripping capacity of 5 mAh cm-2 (a), and the
291
corresponding SEM images of PS-Li-AuLi3@CF (b-d, h-j) and Li@CF (e-g, k-m) electrodes at
292
different stages. 15
293
cm-2 Li was plated on anodes at a current density of 0.5 mA cm-2 and then stripped away. In
294
comparison with Li@CF electrodes, PS-Li-AuLi3@CF electrodes display a more stable voltage
295
plateau, which indicates a better interfacial stability during cycling. Meanwhile,
296
PS-Li-AuLi3@CF electrodes show a smaller voltage hysteresis which is defined as sum of
297
overpotential for Li plating and Li stripping (Fig. 3a). The evolution of surface morphology of
298
PS-Li-AuLi3@CF and Li@CF electrodes during a lithium plating/stripping cycle was studied
299
by SEM after cell disassembly. The SEM images of the electrodes at different stages of cycling
300
are presented as Fig. 3b-m. It is shown that, during the Li plating stages marked with Ⅰ, Ⅰ and
301
Ⅰ, for the PS-Li-AuLi3@CF electrode, Li metal selectively deposits on the AuLi3@CF skeleton,
302
and thus the diameter of the AuLi3@CF is enlarged continuously from about 8 to 12 µm by Li
303
plating (Fig. 3b-d), indicating that the lithiophilic AuLi3 film is able to effectively guide Li
304
metal nucleation and growth. In comparison, Li metal randomly deposits into the interspaces
305
between CFs with a rather dendritic appearance (Fig. 3e-g). Furthermore, during the Li
306
stripping stages marked with Ⅰ, Ⅰ and Ⅰ, for the PS-Li-AuLi3@CF electrodes, the diameter of
307
the AuLi3@CF skeleton gradually reduces (Fig. 3h-j), which indicates that the Li deposit on the
308
AuLi3@CF surface is smoothly eroded. At the final stage of the stripping, the AuLi3@CF
309
surface recovers nearly to its original state as shown in Fig. 1k (Fig. 3j). In contrast, for Li@CF
310
electrodes, although the size of Li dendrites seems to decrease with the progression of stripping
311
(Fig. 3k-m), there is irreversible Li deposition accumulated in the CF matrix. It is noted that
312
there is no growth of Li dendrites on PS-Li-AuLi3@CF electrodes throughout plating/stripping
313
cycles. For Li@CF electrodes, the poor lithiophilicity of the upper part of Li@CF electrodes
314
results in inhomogeneous Li metal nucleation and growth, and a large Li nucleation 16
315
overpotential which can induce Li dendrite growth during Li plating/stripping cycles. These
316
results reveal the significant impact of the lithiophilic AuLi3 modification on Li
317
plating/stripping behavior and suppression of Li dendrite growth, which is in agreement with
318
the previous reports that have utilized other lithiophilic species such as Ag[50], ZnO[39, 40]
319
and SnO2[41] to improve electrochemical performance of LMAs.
320 321
Figure 4. SEM images of (a-c) Li foil, (d-f) Li-AuLi3@CF and (g-l) PS-Li-AuLi3@CF
322
electrodes after cycling for 10 cycles (a, d, g, j), 100 cycles (b, e, h, k) and 150 cycles (c, f, i, l),
323
respectively, at a current density of 0.5 mA cm-2 with a capacity of 1 mAh cm-2 Li.
17
324
In order to investigate the impact of electrode structure on the cycling performance of LMAs,
325
symmetrical coin cells with two identical Li metal electrodes, including Li foils, Li-AuLi3@CF
326
and PS-Li-AuLi3@CF electrodes, were assembled using an electrolyte of 1 mol L-1 LiPF6 in
327
EC/DEC (1:1 vol%) without any additives. Fig. 4 shows SEM images of these Li metal
328
electrodes after cycling for 10 cycles, 100 cycles and 150 cycles, respectively, at a current
329
density of 0.5 mA cm-2 with a capacity of 1 mAh cm-2 Li. The Li foil electrode forms cracks
330
after only 10 cycles (Fig. 4a), and the size of cracks enlarges with the progression of cycling
331
(Fig. 4b, c). Without a host scaffold to minimize the whole-electrode level volume change, the
332
Li plating/stripping process on the Li foil electrode may be constantly mechanically constrained
333
by other inactive cell components such as separator, thus inducing stress fields in Li metal
334
electrode[54], which could cause the electrode to generate cracks. These cracks would
335
destabilize the anode/electrolyte interface, and increase side reactions between Li metal and
336
electrolyte, leading to an unstable and thick SEI which greatly degrades electrochemical
337
performance of LMAs. Although Li deposition shows a denser morphology in the initial stage
338
for Li-AuLi3@CF electrodes without pre-stripping (Fig. 4d), cracks with a smaller size than
339
that of Li foil electrodes still come out after long cycling (Fig. 4e, f), since most part of the
340
AuLi3@CF scaffold is buried inside bulk Li metal at most of the time during Li
341
plating/stripping cycling, which severely restricts the extent of the AuLi3@CF function. In
342
comparison, for PS-Li-AuLi3@CF electrodes (Fig. 4g-i), Li deposit exhibits a uniform, smooth
343
and dense morphology even after cycling for 150 cycles. The higher magnification SEM
344
images reveal that Li metal closely surrounds the AuLi3@CF skeletons (Fig. 4j-l), which is in
345
line with the Li deposition behavior as depicted in Fig. 3. In addition, as shown in Fig. S8, 18
346
morphology evolution of these electrodes after cycling at higher current densities of 1 and 3 mA
347
cm-2 further revealed the structural advantages of PS-Li-AuLi3@CF composites in maintaining
348
the electrode integrity. These results futher verify the effectiveness of the pre-stripping strategy,
349
which functionalizes the exposed portion of AuLi3@CF scaffold and confers cycling stability
350
of Li-AuLi3@CF electrode. It is worth mentioning that a recent study reveals the different
351
cycling behaviors of thin Li foil electrodes with initial plating and stripping. Initial surface
352
morphology, reactive sites and distribution of dead Li are found to govern the following
353
morphology evolution trend during Li plating/stripping process, and subsequently determine
354
the electrochemical performance of LMAs[55]. Hence, further investigation is needed to
355
clarify the difference of cycling behaviors between initially plated and stripped 3D composite
356
LMAs.
357
Based on the above results, the morphology evolution of PS-Li-AuLi3@CF electrodes
358
compared with Li foil and Li-AuLi3@CF electrodes can be schematically illustrated as shown
359
in Fig. 5. For hostless Li foil electrodes, due to large relative volume changes during Li
360
plating/stripping, stress fields exist in the electrode which finally results in formation of cracks.
361
In Li-AuLi3@CF electrodes, since the AuLi3@CF scaffold is buried well inside bulk Li metal,
362
its function should degrade gradually, and the electrode may behave like a Li foil electrode after
363
especially long cycling. In contrast, for PS-Li-AuLi3@CF electrodes, because a portion
364
of AuLi3@CF scaffold has been initially exposed by the pre-stripping protocol, the as-exposed
365
AuLi3@CF scaffold can provide enough void space to accommodate Li plating/stripping. Thus,
366
structural stability of the electrode at a whole-electrode level is maintained, which can
367
significantly weaken the internal stresses in the electrode, and also supply a highly lithiophilic 19
368
AuLi3 interface layer to reduce Li nucleation overpotential and guide uniform Li
369
plating/stripping process, thus suppressing Li dendrite growth.
370 371
Figure 5. Schematic diagram of the morphology evolution on Li foil (left), Li-AuLi3@CF
372
(middle), and PS-Li-AuLi3@CF (right) electrodes.
373 374
In order to evaluate electrochemical performance of LMAs, symmetrical coin cells were
375
assembled with Li foil, Li-AuLi3@CF and PS-Li-AuLi3@CF electrodes, respectively, and
376
cycled at current densities of 0.5, 1 and 3 mA cm-2 with a capacity of 1 mAh cm-2 Li. Fig. 6a
377
compares voltage profiles of the three types of electrodes during cycling at a current density of
20
378 379
Figure 6. Cycling stability of symmetrical coin cells with Li foil, Li-AuLi3@CF and
380
PS-Li-AuLi3@CF electrodes at current densities of 0.5 (a), 1 (b) and 3 (c) mA cm-2 with a
381
capacity of 1 mAh cm-2, respectively. Nyquist plots of impedance spectra of symmetrical
382
PS-Li-AuLi3@CF, Li-AuLi3@CF and Li foil cells after 10 cycles at a current density of 0.5 mA
383
cm-2 (d). Li stripping curve of the PS-Li-AuLi3@CF electrode (e). 21
384
0.5 mA cm-2. The plain Li foil electrodes exhibit a significant increase of Li plating/stripping
385
overpotential until a sudden voltage drop followed by voltage fluctuations appears after cycling
386
for 500 h, which can be attributed respectively to continuous reformation of SEI layer and
387
partial short-circuiting owing to Li dendrite penetration. The Li-AuLi3@CF electrodes show
388
relatively stable cycling for 900 h, which is a great improvement over the Li foil electrodes.
389
After that, however, the Li-AuLi3@CF electrodes exhibit a gradual increase in overpotential.
390
The overpotential of the Li-AuLi3@CF electrodes is ~300 mV after cycling for 1800 h. This is
391
consistent with the SEM observation which reveals that the Li-AuLi3@CF electrode behaves
392
like a Li foil electrode after long cycling. In contrast, the PS-Li-AuLi3@CF electrodes display a
393
much smaller overpotential with a much slower increasing trend than that of Li-AuLi3@CF
394
electrodes during all the cycling. The overpotential of PS-Li-AuLi3@CF electrodes was ~111
395
mV after cycling for 1800 h. At higher current densities of 1 and 3 mA cm-2, PS-Li-AuLi3@CF
396
electrodes also show a more stable cycling behavior with smaller polarizations (Fig. 6b, c).
397
These results clearly demonstrate the advantages from synergistic structure and interface
398
engineering of PS-Li-AuLi3@CF electrodes. In terms of symmetrical cells cycling in an
399
electrolyte of 1 M LiPF6 in EC/ DEC (1:1 vol%) without any additives, PS-Li-AuLi3@CF
400
electrodes deliver one of the best electrochemical performances among the reported 3D
401
composite LMAs (Table. S1). The highly suppressed polarization and more stable cycling are
402
also evidenced by electrochemical impedance spectroscopy (EIS). The corresponding Nyquist
403
plots show that PS-Li-AuLi3@CF electrodes possess the smallest interfacial resistance after 10
404
cycles compared with the plain Li electrodes (Fig. 6d), indicating that the engineered structure
405
and interface of PS-Li-AuLi3@CF electrodes can enable a faster and more stable Li ion 22
406
transport. Besides excellent cycling stability, PS-Li-AuLi3@CF electrodes also maintain their
407
capacity well. Fig. 6e shows that a capacity of about 3041 mAh g-1 (calculated based on the
408
whole electrode weight) can be stripped from a PS-Li-AuLi3@CF electrode when charged to
409
0.5 V, which is equal to about 78.8% of the theoretical capacity of a pure Li metal electrode.
410
Meanwhile, the areal capacity values were also calculated, which were about 30 mAh cm-2 (Fig.
411
S9). The high specific capacity can be ascribed to both light weight of the CF scaffold and
412
pre-stripping of the infused Li metal. Compared with other studies using heavy metallic
413
scaffolds as hosts[36, 56, 57], the AuLi3@CF-based host material presents more promising for
414
fabricating high-performance 3D composite LMAs without significant influence of host weight
415
on the electrode capacity.
416
As shown in Fig. 7, the electrochemical performance of PS-Li-AuLi3@CF electrodes
417
compared with Li foil and Li-AuLi3@CF electrodes was further investigated in full cells
418
employing LiFePO4 (LFP) and sulfurized polyacrylonitrile (SPAN) cathodes, respectively. The
419
Li|LFP and Li|SPAN full cells were cycled at 5C (Fig. 7a) and 2C (Fig. 7b), respectively, for
420
1000 cycles at room temperature. The specific capacity of PS-Li-AuLi3@CF|LFP is about 122
421
mAh g-1 in the first cycle and retains 117 mAh g-1 after 1000 cycles, which is 96.1% of its
422
original capacity, while the specific capacities of Li-AuLi3@CF|LFP and Li|LFP full cells are
423
initially 119 and 118 mAh g-1, and decrease to 90 and 60 mAh g-1 after 1000 cycles,
424
corresponding to a capacity retention of 75.5% and 50.8%, respectively. Meanwhile,
425
PS-Li-AuLi3@CF|SPAN full cell delivers an initial specific capacity of 637 mAh g-1 with a
426
capacity retention of 70.6% after 1000 cycles at 2C, while Li-AuLi3@CF|SPAN and Li|SPAN
427
full cells exhibit an original specific capacity of 683 and 638 mAh g-1 with a capacity retention 23
428 429
Figure 7. Cycling performance of Li foil, Li-AuLi3@CF and PS-Li-AuLi3@CF electrodes in
430
full cells with (a) LiFePO4 (LFP) cathode at 5C, and (b) SPAN cathode at 2C, respectively. (c)
431
Rate capability of Li foil, Li-AuLi3@CF and PS-Li-AuLi3@CF electrodes in full cells with LFP
432
at different rates from 1 to 10 C and (d) the corresponding areal current density with cycling.
433 434
of 23.4% and 27.8% after 1000 cycles at 2C, respectively. It is noted that Li-AuLi3@CF|SPAN
435
and Li|SPAN full cells show comparable specific capacities and a similar degrading trend after
436
200 cycles, suggesting that the AuLi3@CF scaffold has been buried deeply in bulk Li metal,
437
and the Li-AuLi3@CF electrodes begin to behave like Li foil electrodes at that time. Compared 24
438
to Li|LFP full cells with Li foil and Li-AuLi3@CF electrodes, Li|LFP full cell with
439
PS-Li-AuLi3@CF electrodes displays a better rate capability (Fig. 7c). Especially at a higher
440
areal current density of 3.7 mA cm-2 (equal to 10C) (Fig. 7d), a higher specific capacity is
441
attained by the PS-Li-AuLi3@CF|LFP full cell. The above results further demonstrate that the
442
synergistic structure and interface engineering strategy with a pre-stripping protocol to expose a
443
portion of porous scaffold with a lithiophilic surface is of significant importance for boosting
444
the electrochemical performance of 3D composite LMAs fabricated by Li melt-infusion.
445 446
4. Conclusion
447
In summary, we have demonstrated a synergistic structure and interface engineering strategy
448
for 3D composite LMAs, namely “Li-AuLi3@CF” electrodes, which are fabricated by Li
449
melt-infusion into 3D porous CF paper scaffold modified with NPG that converts to AuLi3 after
450
molten Li infusion, through a simple and effective pre-stripping (PS) protocol to initially
451
expose a portion of AuLi3@CF scaffold, yielding “PS-Li-AuLi3@CF” electrodes. Compared
452
with Li foil and Li-AuLi3@CF electrodes, the as-designed PS-Li-AuLi3@CF electrodes
453
maintained structural stability at a whole-electrode level to accommodate huge volume change
454
during Li plating/stripping, and also provided a highly lithiophilic AuLi3@CF interface to
455
guide uniform Li nucleation/growth and suppress Li dendrite growth. These structural and
456
interfacial advantages lead to significantly improved electrochemical performance of
457
PS-Li-AuLi3@CF electrodes. Symmetrical Li|Li cells with PS-Li-AuLi3@CF electrodes can
458
run for 1800 h without cell failure at a current density of 0.5 mA cm-2 with a capacity of 1 mAh
459
cm-2 Li. Furthermore, Li|LFP and Li|SPAN full cells with PS-Li-AuLi3@CF electrodes exhibit 25
460
an excellent capacity retention of 96.1% with a CE of 99.2% at 5C and a capacity retention of
461
70.6% with a CE of 99.8% at 2C for 1000 cycles, respectively. Besides these characteristics,
462
PS-Li-AuLi3@CF electrodes can deliver a relatively high capacity of about 3041 mAh g-1,
463
minimizing the influences of host on the specific capacity. This work provides a new strategy to
464
rationally design and fabricate high-performance 3D composite LMAs based on Li
465
melt-infusion, which shows new avenues for the development of next-generation high energy
466
density rechargeable LMBs.
467 468
Supporting Information
469
Additional optical and SEM images, XRD characterizations, and additional electrochemical
470
measurements.
471 472
Notes
473
The authors declare no competing financial interests.
474 475
Acknowledgments
476
The research was supported by the National Key R&D Program of China (2018YFB0104200).
477 478
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Highlights Nanoporous gold is coated on carbon fibers to improve lithiophilicity. Pre-stripping is conducted for synergistic structure and interface engineering of 3D composite lithium metal anodes. PS-Li-AuLi3@CF electrodes show a specific capacity of about 3041 mAh g-1. Symmetrical Li|Li cells with PS-Li-AuLi3@CF electrodes can run for 1800 h without cell failure at a current density of 0.5 mA cm-2. Boosted electrochemical performance is achieved in Li|LFP and Li|SPAN full cells with PS-Li-AuLi3@CF electrodes.
Declaration of interests ☒ The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper. ☐The authors declare the following financial interests/personal relationships which may be considered as potential competing interests:
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