Abstract:The high Zn ion desolvation energy, sluggish Zn deposition kinetics, and top Zn plating pattern are the key challenges toward practical Zn anodes. Herein, these key issues are addressed by introducing zinc pyrovanadate (ZVO) as a solid zinc-ion conductor interface to induce smooth and fast Zn deposition underneath the layer. Electrochemical studies, computational analysis, and in situ observations reveal the boosted desolvation and deposition kinetics, and uniformity by ZVO interface. In addition, the anti-cor… Show more
“…As portrayed in Figures S15 and S16, the nucleation overpotential (NOP) of Zn reduction increased from 54 mV to 86 mV after introducing the 80 mM Gly additive, and the higher NOP contributed to the formation of finer Zn crystal particles, yielding a compact deposition layer on the anode surface . Thereafter, chronoamperometry (CA) curves (Figure S17) illustrated that the Gly ± adsorbed on the Zn anode’s surface is competent to restrict the Zn 2+ ions’ two-dimensional (2D) diffusion, as shown in Figure f. , Meanwhile, the Gly ± -containing EDL provides a transfer number ( t Zn 2+ ) of 0.59 (Figure S18), much higher than that of the conventional EDL ( t Zn 2+ = 0.23), thus leading to the reasonable conclusion that Gly ± is ideal for reducing the concentration gradient of Zn 2+ at the electrode/electrolyte interface to inhibit uneven deposition caused by locally high Zn 2+ -concentrations. ,, …”
Section: Results
and Discussionmentioning
confidence: 93%
“…63,64 Meanwhile, the Gly ± -containing EDL provides a transfer number (t Zn 2+ ) of 0.59 (Figure S18), much higher than that of the conventional EDL (t Zn 2+ = 0.23), thus leading to the reasonable conclusion that Gly ± is ideal for reducing the concentration gradient of Zn 2+ at the electrode/electrolyte interface to inhibit uneven deposition caused by locally high Zn 2+ -concentrations. 53,65,66 Molecular dynamics (MD) simulations and experimental tests were exploited to investigate the alteration of Zn 2+ solvation structures in Gly-containing electrolytes in this work. The results of MD simulations showed (Figures 4a−b and S19) that Gly ± appeared around the Zn 2+ solvation structure due to coordination between -COO − and Zn 2+ .…”
The
violent side reactions of Zn metal in aqueous electrolyte
lead to sharp local-pH fluctuations at the interface, which accelerate
Zn anode breakdown; thus, the development of an optimization strategy
to accommodate a wide pH range is particularly critical for improving
aqueous Zn metal batteries. Herein, we report a pH-adaptive electric
double layer (EDL) tuned by glycine (Gly) additive with pH-dependent
ionization, which exhibits excellent capability to stabilize Zn anodes
in wide-pH aqueous electrolytes. It is discovered that a Gly-ionic
EDL facilitates the directed migration of charge carriers in both
mildly acidic and alkaline electrolytes, leading to the successful
suppression of local saturation. It is worth mentioning that the regulation
effect of the additive concentration on the inner Helmholtz plane
(IHP) structure of Zn electrodes is clarified in depth. It is revealed
that the Gly additives without dimerization can develop orderly and
dense vertical adsorption within the IHP to effectively reduce the
EDL repulsive force of Zn2+ and isolate H2O
from the anode surface. Consequently, they Zn anode with tunable
EDL exhibits superior electrochemical performance in a wide range
of pH and temperature, involving the prodigious cycle reversibility
of 7000 h at Zn symmetric cells with ZnSO4-Gly electrolytes
and an extended lifespan of 50 times in Zn symmetric cells with KOH-Gly
electrolytes. Moreover, acidic Zn powder||MnO2 pouch cells,
and alkaline high-voltage Zn||Ni0.8Co0.1Mn0.1O2 cells, and Zn||NiCo-LDH cells also deliver
excellent cycling reversibility. The tunable EDL enables the ultrahigh
depth of discharge (DOD) of 93%. This work elucidates the design of
electrolyte additives compatible in a wide range of pH and temperature,
which might cause inspiration in the fields of practical multiapplication
scenarios for Zn anodes.
“…As portrayed in Figures S15 and S16, the nucleation overpotential (NOP) of Zn reduction increased from 54 mV to 86 mV after introducing the 80 mM Gly additive, and the higher NOP contributed to the formation of finer Zn crystal particles, yielding a compact deposition layer on the anode surface . Thereafter, chronoamperometry (CA) curves (Figure S17) illustrated that the Gly ± adsorbed on the Zn anode’s surface is competent to restrict the Zn 2+ ions’ two-dimensional (2D) diffusion, as shown in Figure f. , Meanwhile, the Gly ± -containing EDL provides a transfer number ( t Zn 2+ ) of 0.59 (Figure S18), much higher than that of the conventional EDL ( t Zn 2+ = 0.23), thus leading to the reasonable conclusion that Gly ± is ideal for reducing the concentration gradient of Zn 2+ at the electrode/electrolyte interface to inhibit uneven deposition caused by locally high Zn 2+ -concentrations. ,, …”
Section: Results
and Discussionmentioning
confidence: 93%
“…63,64 Meanwhile, the Gly ± -containing EDL provides a transfer number (t Zn 2+ ) of 0.59 (Figure S18), much higher than that of the conventional EDL (t Zn 2+ = 0.23), thus leading to the reasonable conclusion that Gly ± is ideal for reducing the concentration gradient of Zn 2+ at the electrode/electrolyte interface to inhibit uneven deposition caused by locally high Zn 2+ -concentrations. 53,65,66 Molecular dynamics (MD) simulations and experimental tests were exploited to investigate the alteration of Zn 2+ solvation structures in Gly-containing electrolytes in this work. The results of MD simulations showed (Figures 4a−b and S19) that Gly ± appeared around the Zn 2+ solvation structure due to coordination between -COO − and Zn 2+ .…”
The
violent side reactions of Zn metal in aqueous electrolyte
lead to sharp local-pH fluctuations at the interface, which accelerate
Zn anode breakdown; thus, the development of an optimization strategy
to accommodate a wide pH range is particularly critical for improving
aqueous Zn metal batteries. Herein, we report a pH-adaptive electric
double layer (EDL) tuned by glycine (Gly) additive with pH-dependent
ionization, which exhibits excellent capability to stabilize Zn anodes
in wide-pH aqueous electrolytes. It is discovered that a Gly-ionic
EDL facilitates the directed migration of charge carriers in both
mildly acidic and alkaline electrolytes, leading to the successful
suppression of local saturation. It is worth mentioning that the regulation
effect of the additive concentration on the inner Helmholtz plane
(IHP) structure of Zn electrodes is clarified in depth. It is revealed
that the Gly additives without dimerization can develop orderly and
dense vertical adsorption within the IHP to effectively reduce the
EDL repulsive force of Zn2+ and isolate H2O
from the anode surface. Consequently, they Zn anode with tunable
EDL exhibits superior electrochemical performance in a wide range
of pH and temperature, involving the prodigious cycle reversibility
of 7000 h at Zn symmetric cells with ZnSO4-Gly electrolytes
and an extended lifespan of 50 times in Zn symmetric cells with KOH-Gly
electrolytes. Moreover, acidic Zn powder||MnO2 pouch cells,
and alkaline high-voltage Zn||Ni0.8Co0.1Mn0.1O2 cells, and Zn||NiCo-LDH cells also deliver
excellent cycling reversibility. The tunable EDL enables the ultrahigh
depth of discharge (DOD) of 93%. This work elucidates the design of
electrolyte additives compatible in a wide range of pH and temperature,
which might cause inspiration in the fields of practical multiapplication
scenarios for Zn anodes.
“…By performing EIS, fitted with an equivalent circuit (Fig. S10†) with ZSimpWin software, R ct at different temperatures (Table S5†) can calculate E a , which represents the de-solvation energy barrier, according to the equation: 34–36 where R ct , A , E a , R , and T represent the charge transfer resistance, pre-exponential factor, activation energy, molar gas constant, and absolute temperature. In Fig.…”
Section: Resultsmentioning
confidence: 99%
“…By performing EIS, fitted with an equivalent circuit (Fig. S10 †) with ZSimpWin software, R ct at different temperatures (Table S5 †) can calculate E a , which represents the de-solvation energy barrier, according to the equation: [34][35][36] ln R ct…”
Section: Performance Of Zibs In a Symmetrical Configurationmentioning
Zinc (Zn) is an excellent material for use as anodes for rechargeable batteries in water-based electrolytes. Nevertheless, the high activity of water leads to Zn corrosion and hydrogen evolution, along...
“…After cycling, a significant amount of the Zn 4 SO 4 (OH) 6 •xH 2 O by-products with a hexagonal plate structure was observed on the Zn surface in the BE electrolyte. [42][43][44][45] This indicates that CTAB effectively inhibits the formation of by-products, leading to a more stable electrolyte system. Furthermore, the ratio of I (002) to I (101) increases from 0.80 to 1.66 with the addition of 0.2 m CTAB, indicating a preference for Zn 2+ deposition on the (002) plane in the 0.2 m CTAB-ZS electrolyte (Figure 2c).…”
Section: Study Of Highly Reversible Zinc Plating/strippingmentioning
The practicality of aqueous zinc ion batteries (AZIBs) for large‐scale energy storage is hindered by challenges associated with zinc anodes. In this study, a low‐cost and multi‐function electrolyte additive, cetyltrimethyl ammonium bromide (CTAB), is presented to address these issues. CTAB adsorbs onto the zinc anode surface, regulating Zn2+ deposition orientation and inhibiting dendrite formation. It also modifies the solvation structure of Zn2+ to reduce water reactivity and minimize side reactions. Additionally, CTAB optimizes key physicochemical parameters of the electrolyte, enhancing the stability of the electrode/electrolyte interface and promoting reversibility in AZIBs. Theoretical simulations combined with operando synchrotron radiation‐based in situ Fourier transform infrared spectra and in situ electrochemical impedance spectra further confirm the modified Zn2+ coordination environment and the adsorption effect of CTAB cations at the anode/electrolyte interface. As a result, the assembled Zn‐MnO2 battery demonstrates a remarkable specific capacity of 126.56 mAh g−1 at a high current density of 4 A g−1 after 1000 cycles. This work highlights the potential of CTAB as a promising solution for improving the performance and practicality of AZIBs for large‐scale energy storage applications.
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