| Literature DB >> 35049537 |
Sharmin Sultana1, Kumkum Ahmed2, Prastika Krisma Jiwanti3, Brasstira Yuva Wardhana3, M D Nahin Islam Shiblee4.
Abstract
Ionic liquids (ILs) are molten salts that are entirely composed of ions and have melting temperatures below 100 °C. When immobilized in polymeric matrices by sol-gel or chemical polymerization, they generate gels known as ion gels, ionogels, ionic gels, and so on, which may be used for a variety of electrochemical applications. One of the most significant research domains for IL-based gels is the energy industry, notably for energy storage and conversion devices, due to rising demand for clean, sustainable, and greener energy. Due to characteristics such as nonvolatility, high thermal stability, and strong ionic conductivity, IL-based gels appear to meet the stringent demands/criteria of these diverse application domains. This article focuses on the synthesis pathways of IL-based gel polymer electrolytes/organic gel electrolytes and their applications in batteries (Li-ion and beyond), fuel cells, and supercapacitors. Furthermore, the limitations and future possibilities of IL-based gels in the aforementioned application domains are discussed to support the speedy evolution of these materials in the appropriate applicable sectors.Entities:
Keywords: battery; capacitor; fuel cell; ionic gel; ionic liquid
Year: 2021 PMID: 35049537 PMCID: PMC8774367 DOI: 10.3390/gels8010002
Source DB: PubMed Journal: Gels ISSN: 2310-2861
Figure 1(a) FESEM image of the surface of IE-T electrolyte; (b) FESEM image of the cross-section of IE-T electrolyte; (c,d) FESEM images of the IE-T electrolyte sample after ionic liquid has been extracted; (e) FESEM image of the surface of IE-B electrolyte; (f) FESEM image of the IE-B sample after ionic liquid has been extracted; (g) photograph of IE-T electrolyte and schematic of internal microscopic three-dimensional structure of ionogel. Reprinted with permission from ref. [30].
Figure 2(a) Synthesis HP-A and IL-based gel from HP-A by photopolymerization [44] and (b) basic overview of polymer/inorganic hybrid electrolyte (HE) [34].
Figure 3(a) Locking 1-ethyl-3-methylimidazolium dicyanamide (EMIMDCA) IL in poly(2-acrylamido-2-methyl-1-propanesulfonic acid) (PAMPS)-based DN network through electrostatic interactions [70,71]. (b) Forming polyimide ionogels by solution displacement attributed to hydrogen bonding [72]. (c) Locking EMIMTFSI IL into the PEA elastomer network through hydrogen bonding [39]. (d) The thiol–ene click reaction for preparing DN click ionogel [68].
The difference between GPE and OIG.
| GPE | OIG |
|---|---|
| + solid or semisolid phase | + solid-like phase |
Figure 4Schematic illustration of (a) spin-coating of TMOS/VTEOS IL-based gel electrolyte. (b) GV measurements of different electrolytes on LFP at C/10. Results are shown for gel 1 and gel 2, with the ionic liquid electrolyte (ILE) serving as a comparison (A). The inset shows the dQ/dV versus V curves extrapolated from the GV measurements. (b) Capacity variation with cycling for gel 1. Majority of the 150 cycles were at C/2 (B). Capacity variation with cycling for gel 2. Majority of the 80 cycles were at C/2 (C). Reprinted with permission from ref. [20].
Figure 5Proportion regulation and optimization of components in Na-IL/P(VDF–HFP)@SBA-15: (a) ternary phase diagram of Na-IL/PVDF–HFP@SBA-15 with different X and Y values; X, mass ratios of Na-IL/SBA-15; Y, mass ratios of PVDF–HFP/SBA-15; (b) digital photographs of Na-IL/PVDF–HFP@SBA-15 with X = 2.3, 2.7, 3.0 (fixed Y = 0) and Y = 0.1, 0.2, 0.3 (fixed X = 2.7); (c,d) ionic conductivity of Na-IL/P(VDF–HFP)@SBA-15 corresponding to different ratios of Na-IL/SBA-15 and different ratios of PVDF–HFP/SBA-15 at room temperature, with fixed Y = 0 and X = 2.7, respectively; (e) cycle performance of Na| Na-IL/PVDF–HFP@SBA-15|NVP at 0.1 C (30 °C). Reprinted with permission from ref. [69].
Figure 6Preliminary battery operation using the IL–GPE in a Ca3Co4O9–V2O5 full cell. (a) Galvanostatic charge and discharge curves, attaining discharge capacities reaching 140 mAh/g in the first cycle. The inset shows a stack of three–coin cells powering a small green LED. (b) Plot of discharge capacity vs. cycle number. The inset shows charge–discharge voltage over 25 cycles. Reprinted with permission from [40].
Electrochemical performances of IL-based gel electrolytes for applications in batteries.
| Battery | Cathode | IL-Based Gel | Anode | Preparation Process | Lifecycles | Stability Window | Power and Energy Density | Ionic Conductivity | Refs. |
|---|---|---|---|---|---|---|---|---|---|
| ACP battery | EMIMCl-AlCl3 (neutral) | EMIMCl-AlCl3-PEO | Lewis acid | Magnetic stirrer | 260 mAh g−1, reaches its maximum at 50 cycles | ≤4-≤5 volt | 598 Wh/kg and 374 W/kg | - | [ |
| Na-ion battery | Na3V2(PO4)3 | P(VDF-HFP)/Pyr13FSI-NaTFSI | Metallic Na | Mechanical ball milling, roller pressing | 101.8 mAh g−1, 300 cycles | Up to 4.8 volt | - | 2.48 mS cm−1 at 30 °C | [ |
| Na-ion micro-battery | Na3V2(PO4)3 | NTO/NaBF4-IE/NVP | NTO | Electrochemical deposition | 30.7 mAh cm−3, 3000 cycles | 1–5 volt | 4 W/cm3 and 55.6 mWh/cm3 | 0.18 mS cm−1 at 30 °C | [ |
| Ca-ion battery | Ca3Co4O9/carbon/PVDF binder in NMP solvent | EMITFMS/PEGDA-CQ/4OPP-HFA | Vanadium oxide/carbon/PVDF binder in pure copper foil (cleaned with NMP) | Light emitting diode | 140 mAh g−1, 25 cycles | ≤3 volt | - | Between 1 and 0.1 mS cm−1 at up to 300 °C | [ |
| Solid-state all-organic battery | PTMA | BMIMTFSI/mPEG-MA | Poly(TCAQ) | UV-initiated polymerization | 17 mAh g−1, 1000 cycles | 1 V | - | Up to 0.1 mS cm−1 at room temperature | [ |
| Li-ion battery | LiFePO4 | TMOS/VTEOS | Li | Spin-coating | 125 mAh g−1, 150 cycles | 4 V | 203.15 W/kg and 406.3 Wh/kg | - | [ |
| LiFeO4 | PVDF/PVA/NNBI | Li | Casting method | 104.6 mAh g−1, more than 95% efficiency after 99 cycles | 4.2–2.5 V | - | 1.19 mS cm−1 | [ | |
| LiFePO4 | P(VDF-HFP)/TAIC/EMIMTFSI | Li | EBI | Max 64.1 mAh g−1, still 30.6 mAh g−1 after 30 cycles | 2–4.5 V | - | - | [ | |
| LiFePO4 | P(VDF-HFP)(Pyr13TFSI)/(LiTFSI)(Pyr13TFSI) | Li | Nonsolvent induced phase separation method | 161.9 mAh g−1, 200 cycles | 4.7 V | - | 0.8 mS cm−1 | [ | |
| LiFePO4 | P(VDF-HFP)/(PEGMEMA)(MMA)(OVPOSS)-(PC)(ZnONP) | Li | High-speed stirring, UV radiation | 145 mAh g−1, 100 cycles | 0.5–4.2 V | - | 1.4 mS cm−1 | [ | |
| LiFePO4 | HP-A/BMIMBF4/PVDF/LiBF4 | Li | Photopolymerization synthesis, solution casting | 153.1 mAh g−1, maintained 98.1% after 100 cycles | 4.3 V | - | From 1.2 mS cm−1 at 20 °C to 50 mS cm−1at 120 °C | [ | |
| LiFePO4 | IE-T | Li | Rapid sol–gel method | 142 mAh g−1, 100 cycles | 2.5–4.2 V | - | 1.21 mS cm−1 at 30 °C | [ | |
| IE-B | 140 mAh g−1, 100 cycles | 1.19 mS cm−1 at 30 °C | |||||||
| LiFePO4 | PDEIm/P(VDF-HFP | Li | Simple and scalable phase inversion method | 138.4, mAh g−1, 200 cycles | 4.2 V | - | 1.78 mS cm−1 at 25 °C | [ | |
| LiFePO4 | Li-TFSI/TEOS/(BMP)(TFSI) | Li | Sol–gel method | 140 mAh g−1, 30 cycles | 4.3 V | - | 0. 34 mS cm−1 | [ | |
| LiFePO4 | P(VDF-HFP)-NMP/Pyr13TFSI/LiTFSI | Li | NIPS | 161,9 mAh g−1, 200 cycles | 4.7 V | - | 0.8 mS cm−1 at 25 °C | [ | |
| LiCoO2 | TMPTMA/(LiTFSI)(TBMA-TFSI-DMC) | Li | In situ thermal polymerization | 149 mAh g−1 after 100 cycles | 5.3 V | - | 6.15 mS cm−1 at 25°C | [ | |
| LiFePO4 | P(VDF-HFP)/LiTFSI/PMPyrrTFSI | Li | Slurry-casting method | 148.1 mAh g−1 after 100 cycles | Up to 5.6 V | - | 6.93 mS cm−1 at 25°C | [ | |
| Li-metal battery | LiCoO2 | P(VDF-HFP)/SiO2-(butanon)(NMP)- (EMIMTFSI/EC/PC) | Li | Electrodeposition | 120 mAh g−1, 100 cycles | 5 V | - | 1.11 mS cm−1 at 25 °C | [ |
| LiFePO4 | LiTFSI-EMIMTFSI-P(VDF-HFP) | Li-S | Melt diffusion method | 867 mAh g−1, 200 cycles | 4.5 V | - | 0.88 mS cm−1 at room temperature | [ | |
| Li3V2(PO4)3 | PIL-GF-[EtO(CH2)2MMI]TFSI | Li | Electrodeposition | 46 mAh g−1, 1000 cycles | 3–4.3 V | - | 0.56 mS cm−1 at room temperature | [ | |
| Li-polymer battery | Li2CuO2-LNMC | P(VDF-HFP)/PYR13FSI/LiTFSI | Li | Evaporation in dry box | 90 mAh g−1, 100 cycles | 4.3 V | - | 1.6 mS cm−1 at 30 °C | [ |
| Li–oxygen battery | LiTFSI in EMIMTFSI | PMMA/(MPSP)(EMIM-TFSI) | Li | Thermal curing | 90 mAh g−1, 20 cycles | 1 V | - | 0.54 mS cm−1 | [ |
| Cu electrode | - | (TetraPEG) (LiTFSA/P2225/TFSA | - | Salting-in | - | Up to 4.2 V | - | - | [ |
Figure 7(a) TGA showing the thermal stability of the pristine IL and of the IL–based gel; (b) conductivity versus temperature; (c) DSC profiles of the IL and of the IL-based gel; (d) N2 adsorption/desorption isotherm; inset: BJH pore size distribution for the IL-based gel after IL extraction. Galvanostatic cycling with potential limitation (GCPL) data at room temperature (e,g) and 100 °C (f,h) for EDLCs using IL (a,b) and IL-based gel electrolytes (c,d); insets: CV at 20 mV s−1 recorded after every 1000 GCPL cycles; at the 25,000th cycle, the charge efficiency is 78, 85, 73, and 83% for e, f, g, and h, respectively. Reprinted with permission from ref. [29].
Electrochemical performances of various IL-based gels in different SCs.
| SCs | IL-Based Gel | Preparation Process | Electrodes Used | Lifecycles and Capacity Retention | Stability Window | Specific Capacitance | Power and Energy Density | Ionic Conductivity | Refs. |
|---|---|---|---|---|---|---|---|---|---|
| EDLCs | EMIMTFSI/TMOS/DMDMS | Sol–gel method | AC | 25,000 at 100 °C and 92% | 0–3 V | 177 mF cm 2 at 25 °C | - | 4 mS cm−1 at 20 °C and 26 mS cm−1 at 100 °C | [ |
| BMIMPF6/DVIMBr/HEMA | Thermal polymerization | CNTs | - | 3 V | 1.5–3 mF cm−2 | - | 0.3 to 0.07 mS cm−1 | [ | |
| EMIMBF4/P(VDF-HFP) | Solution casting | rGO | 12,000 cycles and 90% | - | 242 F g−1 at 5 mV s−1 | 33 kW kg−1 and 92 Wh kg−1 | 140 mS cm−1 | [ | |
| BMIMTFSI/PVA/CH3COONH4 | Solution casting | CNTs | 3.3 V | 3.36 F g−1 | 11.37 kW kg−1 and 0.17 W h kg−1 | 2.37 ± 0.02 mS cm−1 at 120 °C | [ | ||
| BMIMBF4/PVDF-HFP/SN/ | Solution casting | AC | 10,000 cycles and ~ 80% | −2.9–2.5 V | 176 F g−1 at 0.18 A g−1 and 138 F g−1 at 8 A g−1 | - | 0.5 mS cm−1 at −30 °C to 15 mS cm−1 at 80 °C | [ | |
| LICs | P(VDF-HFP)/EMIMBF4/LiTFSI | Solution casting | NiO/rGO as the anode and AC as thecathode | 4000 cycles and 83% | 0–4 V | 56.7 F g−1 | 0.8685 kW kg−1 and 49 Wh kg−1 | - | [ |
| Glycidyl-POSS in 1 M LiTFSI/BMPTFSI | Thermal polymerization | AC | 100 cycles and 81% | 5 V vs. Li/Li+ | - | - | 0.701 mS cm−1 at 30 °C | [ | |
| EMIMTFSI/LiTFSI/P(VDF-HFP) | Solution casting | AC | 10,000 cycles and 93.7% | 0–4 V | 68.3 F g−1 | 2.47 kW kg−1 and 147.2 Wh kg−1 at 60 °C | - | [ | |
| (PEO)-co-methacryloxypropyl) silsesquioxane/BMPTFSI/LiTFSI | Thermal polymerization | AC | 50 cycles and 97% | - | - | - | 0.62 mS cm−1 at 30 °C | [ | |
| Solid-state SCs | PVDF-HFP/BMIMI/CNTs | Solution casting | AC | 10,000 cycles and 80.1% | - | 15.7 F g−1 | 0.4599 kW kg−1 and 50.1 Wh kg−1 | 17.6 mS cm−1 | [ |
| polyoxyethylene/nitrile butadiene rubber/EMIMTFSI | In situ polymerization | Graphene | 10,000 cycles and 93.7% | 0–2.5 V | 208 F g−1 at a current density of 1 A g−1 | 5.87 kW h kg−1 and 181 W h kg−1 | 2.4 mS cm−1 at room temperature | [ | |
| polyacrylamide/1-vinyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide | Polymerization | Poly(3,4-ethylenedioxythiophene/carbon cloth | 3000 cycles and 93% | - | 157.8 F g−1 | 14.22 Wh kg−1 | 23 mS cm−1 at 90 °C | [ | |
| Solid-state sodium ion SCs | P(VDF-HFP)/EMIMBF4/NaTFSI | Solution casting | MoS2/CNTs as working electrode and sodium foil used as a counter electrode | 8000 cycles and 81% | 0–3.8 V | - | 2.0909 kW kg−1 and 80 W h kg−1 at 70 °C and | 0.67 mS cm−1 at 20 °C | [ |
| Self-charging SCs | P(VDF-HFP)/TEABF4 | Electrospinning | MoSe2 electrodes | 2500 cycles and 91% | 0–2 V | 18.93 mF cm−2 | 268.91 μW cm−2 and 37.90 mJ cm−2 | [ | |
| Flexible SCs | P(VDF-HFP)/EMIMTFSI | Sol–gel method | Carbon electrode | 10,000 cycles and 99.95% | 0–2.5 V | 118 to 115 F g−1 | 6.25 kW kg−1 and 21.9 W h kg−1 | 8.6 mS cm−1 | [ |
| PHEMA-co-PEGDMA/EMIMBF4 | UV-polymerization | AC | 3500 cycles and 91% | 0–3 V | 193.33 F g−1 at 5 mV s−1 | 1.23 kW kg−1 and 49.55 Wh kg−1 | 12.27 mS cm−1 at room temperature | [ | |
| P(VDF-HFP)/EMIMBF4 | Solution casting | MnO2/CNTs | 10,000 cycles and 88.5% | 3 V | 8.6 F cm−3 | 1804 mWcm−3 and 4.2 mWh cm−3 | - | [ | |
| PVA/boric acid/EMIMCl | Solution casting | AC | 3000 cycles and 98% | 0–1 V | 90 F g−1 | 0.9 kW kg–1 and 12.36 Wh kg–1 | 2.43 mS cm−1 | [ | |
| MSCs | Fumed SiO2/EMIMTFSI | Sol–gel method | Porous carbon | 10,000 cycles and 94% | 2 V | - | 26 W cm−3 and mW h cm−3 | - | [ |
| PVDF/EMIMTFSI | Sol–gel method | 3D MnO2 electrodes | 30,000 cycles and 96.2% | - | 36 mF cm−2 at 20 mV s−1 | 3.8 mW cm−2 and 4.4 μWh cm−2 | - | [ | |
| P(VDF-HFP)/EMIMBF4 | Solution casting | Graphite as working electrode and Pt foil as counter electrode | 5000 cycles and 93% | 3.5 V | 17.4 mF cm−2 | 59 mWh cm−3 | 25 mS cm−1 | [ | |
| PEGDA/EMIMTFSI | UV-polymerization | Multi-walled carbon nanotube (MWCNT) | 30,000 cycles and ~80% | 0–2 V | 5.3 F cm−3 10 mV s−1 | 21.0 W cm−3 and 0.17 mWh cm−3 | 9.4 mS cm−1 | [ | |
| PEO/BMIMTFSI/LiTFSI | Solution casting | CNT microelectrodes | 5000 cycles and 94.4% | 0–3 V | 21 F g−1 | 750 μW cm−2 and 47.88 μWh cm−2 | 4.07 mS cm−1 | [ | |
| Microporous carbon/Fe2O3/EMIMBF4 | 3D printing | Microporous carbon/Fe2O3 | 10,000 cycles and 93.2% | - | 377 F g−1 | - | - | [ |
Figure 8(a) Synthetic route of the polymeric skeleton, (b) the illustration of PG-DHS and PG-MHS IL-based gels, and (c) polarization curves of the H2/O2 fuel cell prepared from PG-MHS at temperatures from 90 to 120 °C. Reprinted with permission from ref. [134].
Figure 9Potential application of IL-based gels in electrochemical devices.