Conventional aqueous electrolytes, influenced by the voltage of water decomposition, show a narrow electrochemical window (~1.23 V) [49]. The water activity will decrease and the electrochemical stability window will enlarge in aqueous electrolytes with the increase in salt concentration [50,51]. Meanwhile, the coordination environment of metal ions can be tuned and the number of solvation water molecules of metal cations can be reduced by employing high-concentration salt. The solvent sheath layer of metal ions is occupied by anions, which reduces the required energy for the desolvation of metal ions. The active water molecules reaching the electrode and electrolyte surface are reduced, which is able to prohibit the evolution of H₂ and the corrosion phenomenon, and inhibit the occurrence of side reactions of the metal anode, effectively promoting the cycle life of ZIBs [52,53].

Given the advantages of low cost, non-toxicity, good solubility, and stable electrochemical properties of zinc sulfate (ZnSO₄) in an aqueous solution, it is regarded as one of the common zinc salts at this stage and widely used in aqueous ZIBs. In the mixed electrolyte (ZnSO₄+MnSO₄), Raman spectra show that the broad peaks indicating free water molecules are gradually suppressed, and Zn⁺-coordinated ambient water molecules are reduced as the electrolyte concentration of ZnSO₄ increases from 2 M to 4.2 M. It is able to restrain side reactions and improve the cyclic stability of zinc metal anodes. A half-cell of Zn||Cu showed low polarization in dilute electrolyte (2 M ZnSO₄ + 0.1 M MnSO₄) with Zn plating/stripping cycles over 1000 h at 0.2 mA cm⁻² current density [54]; the average coulombic efficiency (ACE) for cycling >120 was 97.54%; while in 4.2 M ZnSO₄ and 0.1 M MnSO₄ mixed electrolyte, it was able to reach 99.21%. Another full cell of Zn||MnO₂ showed advanced long-cycle behavior under a measurement of more than 1200 cycles at 938 mA g⁻¹, with an ACE close to 100% and 88.7% capacity retention. The dissolution of the cathode material would be inhibited via addition of MnSO₄ and a synergistic effect with its solvation structure was created to achieve a stable, reversible, and high-performing Zn||MnO₂ full cell [55]. The Zn anode in 3 M ZnSO₄ electrolyte exhibited an impressively advanced coulombic efficiency (>99%) [56], excellent reversibility, as well as good rate capability, achieving >8000 cycles, which significantly prolonged the cycle life of Zn with increasing current density.

Another example of zinc salt is Zn(TFSI)₂ with high electrochemical stability and ionic conductivity. Wang and coworkers [15] introduced the concept of “water-in-salt” in ZIBs for the first time by using the electrolyte with high concentration (20 m LiTFSI + 1 m Zn(TFSI)₂), resulting in an electrolyte pH of 7. According to the FTIR and ¹⁷O−NMR spectra, it can be found that with increase in the concentration of Li ions, the water molecules tend to form solvent sheaths with Li ions more. When the concentration of LiTFSI ≥20 m, the water molecules are strictly confined to the Li ions’ solvation structure, and such a solvent sheath layer of Zn ions is changed from the original partition to be occupied by anions, and TFSI⁻ surrounds Zn²⁺. The altered solvation structure of zinc ions avoids direct contact between the zinc metal anode and the water molecules of the solvent sheath layer, thus significantly inhibiting the HER phenomenon and the formation of by-products. The metallic Zn cathode exhibits superb electrochemical stability and deposition/stripping reversibility. The highly concentrated electrolyte results in dendrite-free zinc plating/stripping of about 100% coulombic efficiency with no observed by-product formation throughout the application. As for another highly concentrated solution with 20 m LiTFSI+ 1 m Zn(OTf)₂ [57], Zn²⁺ prefers to combine with O(TFSI⁻) compared to O(water). Compared with low-concentration electrolytes, it shows good reversibility of galvanizing/zinc stripping, less polarization in long cycles, and long cycle life. It can form a stable SEI film, which makes the galvanized Cu surface uniform and flat. The capacity retention of the Zn||LiMn₂O₄ full cell is 92% with an average CE about 99.62% after 300 cycles. A Zn||P(4VC₈₆-stat-SS₁₄) full cell exhibited an ultra-long lifetime in 4 M Zn(TFSI)₂ electrolyte [58]. A high reversible capacity about 184 mAh g⁻¹ was maintained with a capacity retention rate of 83% after 48,000 continuous cycles.

ZnCl₂ with significant solubility is often chosen as a high-concentration electrolyte. A highly reversible full cell of V₂O₅||Zn was fabricated by Tang et al. [59] with a ZnCl₂ “water-in-salt” electrolyte (WISE) to extend its life at high-temperature storage. V₂O₅ cathodes in dilute electrolytes experience severe lattice swelling from 4.4 to 13.9 Å (319%) due to the co-insertion of hydrated zinc ions, with reduced active material, resulting in capacity loss and reduced cycling performance. An ultrahigh capacity of about 302 mAh g⁻¹ can be achieved by a V₂O₅||Zn full cell with conventional electrolyte (1 M ZnSO₄), and the capacity decreases rapidly. In contrast, cycling in 30 m ZnCl₂ exhibits a maximum capacity of 341 mAh g⁻¹, which shows about a 9.5% decay after 300 cycles, demonstrating ultra-high cycling stability within 1000 cycles. The ZnCl₂ WISE (30 m) can prevent co-insertion of water molecules, and inhibit dissolution of vanadium-based materials, resulting in an expanded electrochemical window, which inhibits the protrusion of zinc dendrites, and improves electrochemical performance. A mixed electrolyte was formed by adding 5 m LiCl to 30 m ZnCl₂, in which hydrogen bonds between H₂O can be broken by Li salt, reduce the free water molecules around Zn²⁺, and limit the solvation process of Zn²⁺ ions to achieve a higher CE of the mixed double-ion (5 m LiCl + 30 m ZnCl₂) WISE than that of a single salt (30 m ZnCl₂) [60]. Zhang and coworkers [61] found that the solubility of ZnCl₂ was able to reach 31 m at room temperature and proposed using a 30 m ZnCl₂ solution as an electrolyte for ZIBs to enhance the reversibility of the Zn anode. Distinct from 5 m ZnCl₂, a symmetric cell of Zn||Zn exhibited excellent cycle stability when plating/stripping at 0.2 mA cm⁻² for 10 min in a 30 m ZnCl₂ electrolyte solution. The viscosity of the electrolyte solution increases with concentration increases and electrical conductivity decreases. However, the ion migration number of Zn²⁺ is higher in the highly concentrated electrolyte than that in the lowly concentrated one. A lower degree of hydrolysis slows down Zn(OH)₂/ZnO formation, and the electrochemical window and pH also increase with concentration, indicating that the hydrolysis of Zn²⁺ is inhibited and inhibits the HER, which brings higher reversibility of the zinc metal anode as well as tunes the uniform deposition of Zn²⁺.

As mentioned above, side reactions and Zn dendrites are the main issues that need to be addressed in ZIBs, which can result in corrosion, HER, and passivation. Different types of functional electrolyte additives can inhibit side reactions and growth of zinc dendrites by different mechanisms. In recent years, the role of additive engineering has been extensively studied in ZIBs.

Tetrabutylammonium sulfate (TBA₂SO₄) is an effective, low-cost, non-toxic cationic surface-activator-type electrolyte additive. Zhu et al. [71] proposed to add TBA₂SO₄ to the 2 M ZnSO₄ electrolyte with a small amount about 0.029 g L⁻¹, and the positively charged TBA⁺ gathered at the negatively charged zinc “bulge” by electrostatic adsorption, forming an electrostatic shield and limiting the tip effect. TBA⁺ causes Zn²⁺ deposition in adjacent flat areas, inducing uniform zinc deposition through a unique zincophobic repulsion mechanism. A full cell of Zn||MnO₂ with TBA₂SO₄ exhibits a cycle stability of about 300 times at 1 A g⁻¹ with a 94% capacity retention. Wang et al. [62] found that by adding 2 v.% of diethyl ether (Et₂O), Zn²⁺ will shift to other regions during zinc deposition. Zn||MnO₂ cells in 0.1 M Mn(CF₃SO₃)₂ and 3 M Zn(CF₃SO₃)₂ mixed aqueous solution with Et₂O as an additive were able to cycle 4000 times at 5 A g⁻¹ with a 97.7% capacity retention rate, showing excellent cycling performance. Because Et₂O molecules can preferentially adsorb on the prominent tip, eliminating the “tip effect” and flattening the zinc anode surface, it can largely restrain growth of zinc dendrites. Guo et al. [63] added a small amount (25 × 10⁻³ M) of Zn(H₂PO₄)₂ salt to 1 M Zn(CF₃SO₃)₂ electrolyte. From the Raman spectrum, it can be seen that SEI−Zn has bonds between Zn and O, and P and O, compared with bare−Zn, which demonstrates the formation of the SEI.

The abovementioned additives can be broadly classified as ionic and nonionic, capable of achieving dendrite-free zinc deposition by electrostatic shielding or by forming SEI films. Improving the performance of ZIBs also requires avoiding side reactions. In the aqueous electrolyte, the stable form of Zn²⁺ is [Zn(H₂O)₆]²⁺ requires high energy for desolvation during the deposition process. Researchers have found that additives can adjust the solvation structure. Replacing H₂O molecules in [Zn(H₂O)₆]²⁺ with other ions or molecules with weaker solvation structure effects can reduce the desolvation energy as well as prevent the side reactions [46].

Much research related to organic substances as common additives already exists. Li et al. [72] added ethylene glycol (EG) to the ZnSO₄ electrolyte and found that it is effective in improving Zn²⁺ reversible deposition. The red-shift in the OH stretches H₂O (3200~3400 cm⁻¹), and OH stretched bending of C−OH (1460~1465 cm⁻¹) shows a blue shift and can be noted from the Raman spectrum, indicating that the electron density of OH in H₂O is lower and the electron density of C−OH in EG is higher, and the hydroxyl group of EG has a solid force to generate hydrogen bonds with H₂O, which can effectively weaken the force between Zn²⁺ and H₂O. Experiments and theoretical calculations show that with the increase in EG content, the OH stretching vibration range from 3000 to 3500 cm⁻¹ can lead to a significant redshift, and H₂O bending vibration in the range of 1600~1700 cm⁻¹ is slightly blueshifted in the FTIR spectrum [73,74]. Pan et al. [75] used ab initio calculations to analyze the solvation energy of different Zn²⁺ solvation sheaths in ethylene glycol/water solutions. They found that the solvation energy was ranked as [Zn(H₂O)_m (EG)_n]²⁺ < [Zn(H₂O)₆ ]²⁺ < [Zn(EG)₃ ]²⁺, indicating that the interaction force between EG and zinc ions was greater than that between Zn²⁺ and water, disrupting the solvation of Zn²⁺ and effectively inhibiting the occurrence of the HER. H₂O in a zinc ion solvation sheath can be replaced by DMSO because of its (29.8) higher Gutmann donor number and larger dielectric constant than that of H₂O (18), and O had a smaller electron density in DMSO [79,80]. With the addition of DMSO, interaction between solvation water and Zn²⁺ can be weakened, which facilitates the desolvation process of zinc ions and can suppress the decomposition of active H₂O, improving the zinc plating and stripping coulombic efficiency. The solvation DMSO can lead to SEI layer formation in situ on the anode surface, which allows passage of zinc ions and hinders the passage of water molecules. The Zn||Zn symmetric cell in such a mixed electrolyte exhibited a cycle life of more than 1000 h. The cycle life was improved by a factor of 2.5 compared to that of the ZnCl₂−H₂O symmetric cell. Zn||Ti half-cells increased the CE to 99.0% and finally 100% within 30 cycles, exhibiting a stable over potential of ~24 mV, confirming the ability of the DMSO additive in improving the CE of plating/stripping. Qiao et al. [81] added 50 v.% methanol to the ZnSO₄ electrolyte. They found that methanol can insert into the internal Zn²⁺ solvation sheath owing to the high dielectric constant and small size (37.2) [82,83] and can disrupt the coordination equilibrium of Zn²⁺ by adjusting the amount of methanol addition. The methanol molecules will first interact with H₂O in the first layer of the Zn²⁺ solvated sheath layer and form hydrogen bonds. In addition, the high wettability between methanol and the Zn metal anode makes it easier for methanol molecules to adsorb on the surface of Zn metal than solvent water, inducing the realization of dendrite-free Zn²⁺ uniform deposition. When the size of methanol molecules becomes larger, they will eventually insert into the inner layer of the Zn²⁺ solvent sheath, the activity of water will decrease, and both hydrogen precipitation reactions and side reactions will be inhibited. Yang et al. [84] demonstrated by introducing N-methyl-2-pyrrolidone (NMP) polar additives to ZnSO₄ that the addition of organic solvents containing carbonyl groups contributes to stabilizing the hydrogen bonding network of water and the structural remodeling of Zn²⁺−solvation, and such a synergistic effect helps to inhibit dendrite formation and water-induced parasitic reactions.

By investigating the influence of different organic additives on the Zn²⁺ solvation structure, researchers have provided an electrolyte regulation approach to achieve highly reversible Zn anodes and cells. Except for organic additives, salt additives are considered as another effective way to promote the electrochemical performance of Zn anode. Zhang et al. [90] used trifluoromethanesulfonate (OTf⁻) anions and ethylenediaminetetraacetic acid (Y⁴⁻) anions to form a mixed electrolyte (BE + 100 mM) consisting of 1 M Zn(OTf)₂ + 100 mM Na₄Y, and the double anion can change the Zn²⁺ solvation sheath to stabilize the Zn anode. In addition, this solvation structure allows decomposition of ligand anions to generate an in situ organic–inorganic SEI on the Zn surface. The resulting Zn²⁺ conducting SEI layer can lead to separation between Zn and the electrolyte, thereby inhibiting side reactions derived from H₂O. As a result, the Zn||Zn cell has a coulomb efficiency of 99.7% at 1.0 mA cm⁻² and 1.0 mAh cm⁻² for more than 1600 h, demonstrating excellent long-term stability. The Zn||Cu cell is highly reversible, possessing a coulomb efficiency of 99.7% at more than 400 cycles at 1.0 mA cm⁻². Chen et al. [91] demonstrated that via adding halogen ions to the Zn²⁺ solvation structure, the issues of dendrite growth and hydrogen precipitation reactions could be overcome. Through electrolyte regulation consisting of ammonium halide and zinc acetate, I⁻ can combine with Zn²⁺ to convert the conventional Zn(H₂O)₆²⁺ to ZnI(H₂O)₅⁺, where I⁻ can transfer electrons to H₂O, and water molecules in the solvation structure would be reduced by inhibiting the reduction in the lowest unoccupied molecular orbital (LUMO) energy level and reducing the electron loss, thus improving the reduction stability and, thus, inhibiting HER. The formation of a dynamic electrostatic shielding layer accompanied with NH₄⁺ can inhibit the growth of dendrites.

In summary, electrolyte additives have obvious effects inhibiting side reactions and dendrites of ZIBs. Significantly, the selection of additives should consider three aspects: (1) Gutmann donor number of solvent additives, which can replace H₂O in the solvation sheath of Zn²⁺ when the donor number is larger than H₂O and can maintain Zn²⁺ ion transfer kinetics to some extent [92]. (2) Interaction with H₂O, which can form hydrogen bonds with H₂O, reduce H₂O activity, and inhibit H₂O reduction. (3) In situ formation of SEI film, which should form a dense, self-healing Zn²⁺-conducting SEI film to prevent water penetration into the zinc anode. Furthermore, the electrolyte additives also have a vital effect on the cathode material. For example, the addition of triethyl phosphate (TEP) in the Zn(OTF)₂-H₂O electrolyte in Zn||V₂O₅ batteries can keep the pH of the electrolyte solution stable and hinder the dissolution of V₂O₅ to some extent, which has strong interactions with Zn²⁺ and H₂O molecules. The TEP will enter the inner layer of the solvation sheath of Zn²⁺ and break the hydrogen bonding network between water molecules, thus reducing the activity of H₂O and avoiding the reaction between V₂O₅ and H₂O [93]. Another report mentioned that introducing polyethylene glycol (PEG) into the electrolyte can reduce the content of free water molecules and inhibit the H⁺ insertion to the LiV₂(PO₄)₃ (LVP) cathode through the strong interaction between PEG and H₂O, which is beneficial for suppressing the phase change of LVP. Significantly, much attention should also be paid to the cathode materials for the development of water-based ZIBs.