| Literature DB >> 36132559 |
Chhail Bihari Soni1, Vipin Kumar1.
Abstract
The rigorous requirements, such as high abundance, cost-effectiveness, and increased storage capacities, pose severe challenges to the existing Li-ion batteries' long-term sustainability. Room-temperature aluminum-sulfur (Al-S) chemistry, in particular, is gaining importance due to its high theoretical energy density (1700 W h kg-1). Al-S battery technology is one of the emerging metal-sulfur candidates that can surpass current Li-ion chemistries. When coupled with sulfur, aluminum metal brings a cheap and energy-rich option to existing battery technologies. Owing to the unique virtues of the Al-S battery, it has garnered increasing interest among scientific communities. Al-S chemistry has been investigated for quite some time, yet the cell performance remained in its infancy, which poses a challenge to this technology's viability. Besides stabilizing the Al metal anode, the most important challenge in the practical development of Al-S batteries is the development of a suitable sulfur cathode material. Owing to the complexity of this multivalent system, numerous factors have been taken into account, but the best sulfur cathode is yet to be identified. A detailed exploration of sulfur cathodes and their implications on the battery performance are discussed in this mini-review article. We present a detailed picture of cathode materials that may serve as the reference guide for developing more practical cathode materials. Also, fundamental principles and challenges encountered in the development of the sulfur cathodes are highlighted. Through the knowledge disseminated in this mini-review, the development in the multivalent post-Li-ion battery can be accelerated. A glimpse of the future outlook on the Al-S battery system with different potential solutions is also discussed. This journal is © The Royal Society of Chemistry.Entities:
Year: 2021 PMID: 36132559 PMCID: PMC9417845 DOI: 10.1039/d0na01019g
Source DB: PubMed Journal: Nanoscale Adv ISSN: 2516-0230
Fig. 1Schematic representation of the macroscopic and microscopic view of the Al–S battery.
Fig. 2Schematic illustration of the progress made in the materials chemistry of the cathode to achieve a reversible Al–S battery.
Fig. 3(a) A typical charge/discharge curve of the Al/S battery at room temperature with the ACC/S cathode, ionic-liquid electrolyte, and the Al foil anode. Current: 50 mA g−1. (b) Cycling stability of the Al/S cell.[53] Reproduced with permission. Copyright 2016 John Wiley and Sons. (c) Discharge and charge capacities, and the coulombic efficiencies as a function of the cycle number for the cell, (d) pristine Al foil, and from Al foils immersion in the (e) electrolyte without HCl, and in (f) the electrolyte containing 0.02 M HCl for 24 h.[24] Reproduced with permission. Copyright 2020 Royal Society of Chemistry. (g) Schematic illustrating the preparation process of S@HKUST-1-C.[57] Reproduced with permission. Copyright 2019 John Wiley and Sons.
Fig. 4(a) Schematic of an electrode (cathode)–separator assembly for a non-aqueous room-temperature Al–S battery. (b) Scanning electron microscope (SEM) image of a single-wall carbon nanotube (SWCNT) coating on a glass fiber separator. (c) SEM image of a carbon nanofiber (CNF) matrix. Voltage versus time profiles of (d) an Al‖SWCNT–GF‖S cell (up) and Al‖GF‖S cell at C/20 rate (down). (e) Discharge capacities as a function of the cycle number of the Al‖SWCNT–GF‖S and the Al‖GF‖S cells at the C/20 rate. (f) Voltage profiles of the Al‖SWCNT–GF‖S cell at various C rates. (g) Cyclic voltammetry profiles (at the first, second, fourth, sixth, and eighth cycle) of the Al‖SWCNT–GF‖S cell at a scan rate of 0.03 mV s−1. (h) X-ray diffraction (XRD) patterns of a CNF matrix, a fresh CNF/S electrode and a CNF/S electrode upon a discharge–charge cycle, respectively.[48] Reproduced with permission. Copyright 2017 John Wiley and Sons.
Fig. 5(a) Voltage profiles of the SWCNT/S cathode (left) and comparison of the SWCNT/S cathode cycling stability with different voltage limits (right).[50] Reproduced with permission. Copyright 2020 American Chemical Society. (b) Schematic representation of the mechanism of the Li-ion mediated IL electrolyte (up). (c) Discharge capacities and coulombic efficiencies as a function of the cycle number for the Al‖Li+–Al[EMI]Cl4‖S cell and the Al‖Al[EMI]Cl4‖S cell.[49] Reproduced with permission. Copyright 2018 Elsevier.
Fig. 6(a) The cycling performance and the coulombic efficiency at a current density of 100 mA g−1. (b) The cycling performance at a current density of 200 mA g−1.[33] Reproduced with permission. Copyright 2016 John Wiley and Sons. (c) Schematic illustration of the formation process of NiS nanobelts. (d) The cycling performance and the coulombic efficiency at a current density of 200 mA g−1. (e) The rate cycling performances of the NiS nanobelts.[86] Reproduced with permission. Copyright 2016 Royal Society of Chemistry.
Fig. 7Electrochemical performance of SPAN in Al–S battery applications. (a) Cyclic voltammograms, (b) cycle performance, (c) galvanostatic (dis-)charge curve, (d) rate capabilities.[98] Reproduced with permission. Copyright 2018 American Chemical Society.
Sulfur cathode materials explored for room-temperature Al–S batteries
| S. no. | Material system | Synthesis route | Initial discharge capacity (mA h g−1) | Discharge (mA h g−1) at ∼ | Advantage | Disadvantage |
|---|---|---|---|---|---|---|
| 1 | Ketjen black carbon/S[ | Solution-processed slurry based method | 1200 @ 120 mA g−1 | <50 after 4 cycles | High energy density (1700 W h kg−1) | Inability to oxidize AlS |
| 2 | Activated carbon cloth/S[ | Melt diffusion method | 1320 @ 50 mA g−1 | 1000 @ 20th cycles | Improved reversibility | Large voltage hysteresis, slow solid-state sulfur conversion reaction, and low cycle efficiency (20 cycles) |
| 3 | S@CMK-3 (ref. | Melt diffusion method | 1390 @ 251 mA g−1 | >400 after 20 cycles | Enhanced charge/discharge kinetics and high S-utilisation of 82% | Short cycle life (20 cycles) and polysulfide diffusion |
| 4 | Carbonised-ZIF/S[ | Solvothermal synthesis | 1410 @ 200 mA g−1 | 420 after 30 cycles | Passivation of Al anode and inhibition of hydrolysis of AlS | Large voltage hysteresis and low S-loading (0.2 mg cm−2) |
| 5 | S@HKUST-1-C[ | Hydrothermal method | 1200 @ 1000 mA g−1 | 460 @ 500th cycles | Improved reversibility and enhanced cycle efficiency | Reduced utilization of sulfur |
| 6 | S[ | Commercial S-powder | 113.64 @ 15 mA g−1 | 104.69 after 40 cycles | Improved performance of the electrolyte | Low discharge capacity and loss of sulfur |
| 7 | CNF/S as cathode & SWCNT coated separator[ | Vacuum filtration and vacuum drying | >1200 @ 0.05C | >450 after 10 cycles | Reduced polarization and alleviate polysulfide diffusion | Low S-loading (1 mg cm−2) |
| 8 | SWCNT/S[ | Nondestructive sublimation–deposition method | >900 @ 100 mA g−1 | 1024 @ 2nd cycle | Improved charge transfer kinetics | Capacity decay |
| 9 | CNF/S as cathode & SWCNT-coated GF separator[ | Vacuum filtration and vacuum drying and activation process | ∼1000 @ 0.05C | 600 after 50 cycles | Enhanced reversibility and suppressed formation of Al | Low sulfur-loading (1 mg cm−2) |
| 10 | Mo6S8 (ref. | Chemical intercalation process | 148 @ 12 mA g−1 | 70 after 50 cycles | Good cyclic stability | Low discharge capacity |
| 11 | Ni3S2/graphene micro flakes[ | Mixing | 350 @ 100 mA g−1 | 60 after 100 cycles | High discharge voltage plateau (≈1.0 V | Side reactions due to the dissociation process of complex-ions (Al2Cl7−) |
| 12 | NiS[ | Hydrothermal method | 104.7 @ 200 mA g−1 | 100 after 100 cycles | Facilitation of the electrolyte immersion and enhancement of Al3+ diffusion, high storage capacity, good cyclability and low overpotential | Low cell voltage plateau (∼1.15 V |
| 13 | Graphene/CoS2/S as cathode & rGO coated separator[ | Melt diffusion method and hydrothermal method | 680 @ 50 mA g−1 | 1145 after 37 cycles | Suppress polysulfide diffusion and decrease polarisation | Low sulfur loading of 0.2–0.4 mg cm−2 |
| 14 | SPAN[ | Thermal polymerization | 343 @ 0.025 mA g−1 | 201 after 20 cycles | Superior rate capacities | Low cycle life and low S-loading (1.5 mg cm−2) |
| 15 | Co3S4 (ref. | Solvothermal process | 287.9 @ 50 mA g−1 | 90 after 150 cycles | Good rate performance | Rapid capacity loss and limited current density |
Fig. 8Advancing Al–S batteries through the design of a next-generation sulfur cathode and introduction of kinetic promoters.
Fig. 9(a) Schematic illustration for the synthesis of sulfur nanospheres and sulfur nanospheres@ultrathin δ-MnO2 nanosheet core–shell structures, and the conversion of Li2S on the core–shell surface.[101] Reproduced with permission. Copyright 2020 American Chemical Society. (b) Catalytic mechanism of SACs for sulfur electrodes.[102] Reproduced with permission. Copyright 2021 Elsevier.