CIESC Journal ›› 2024, Vol. 75 ›› Issue (4): 1222-1240.DOI: 10.11949/0438-1157.20231268
• Reviews and monographs • Previous Articles Next Articles
Yunxuan LI1(), Xinyue LIU1(), Xi CHEN2, Wen LIU2, Mingyue ZHOU1(), Xingying LAN1
Received:
2023-12-04
Revised:
2024-03-04
Online:
2024-06-06
Published:
2024-04-25
Contact:
Mingyue ZHOU
李云璇1(), 刘新悦1(), 陈熙2, 刘文2, 周明月1(), 蓝兴英1
通讯作者:
周明月
作者简介:
李云璇(2001—),女,硕士研究生,2654336380@qq.com基金资助:
CLC Number:
Yunxuan LI, Xinyue LIU, Xi CHEN, Wen LIU, Mingyue ZHOU, Xingying LAN. Energy storage technologies based on solid-liquid redox-targeting reactions: materials, devices, and kinetics[J]. CIESC Journal, 2024, 75(4): 1222-1240.
李云璇, 刘新悦, 陈熙, 刘文, 周明月, 蓝兴英. 基于固液氧化还原靶向反应的能量存储技术:材料、器件及动力学[J]. 化工学报, 2024, 75(4): 1222-1240.
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Fig.1 (a) Schematic diagram of RFB[7];(b) Schematic diagram of RTFB; (c) The redox-targeting reaction principle of freely diffusing shuttle molecules S and insulating electrode materials such as LiFePO4[8]; (d) Energy diagram and charge transfer of SMRT reaction between RM+ and LiFePO4[9]
场景 | 电对的作用 | 电对的溶解度要求 | 电对与电池性能关联 |
---|---|---|---|
常规RFB | 储能介质 | 大于1 mol/L | 决定能量密度、功率性能 |
氧化还原靶向RFB | 传递能量+储能 | 大于0.05 mol/L | 决定功率性能 |
Table 1 Characteristics of redox pairs in conventional RFB and RTFB
场景 | 电对的作用 | 电对的溶解度要求 | 电对与电池性能关联 |
---|---|---|---|
常规RFB | 储能介质 | 大于1 mol/L | 决定能量密度、功率性能 |
氧化还原靶向RFB | 传递能量+储能 | 大于0.05 mol/L | 决定功率性能 |
Fig.2 (a) Redox potential of metal ions[16]; (b) Comparison of redox potential and equivalent electron concentration of organic small molecules[33]; (c) Redox potential of intercalation materials
指标 | 全钒 电池[ | 铁铬 电池[ | 锌铁 电池[ | 锌溴 电池[ |
---|---|---|---|---|
能量密度①/(W·h/L) | 约39.5 | 约31.2 | 约25.4 | 65 |
能量效率/% | 83 | 70~75 | 83 | 80 |
Table 2 Electrochemical performance of traditional flow batteries
指标 | 全钒 电池[ | 铁铬 电池[ | 锌铁 电池[ | 锌溴 电池[ |
---|---|---|---|---|
能量密度①/(W·h/L) | 约39.5 | 约31.2 | 约25.4 | 65 |
能量效率/% | 83 | 70~75 | 83 | 80 |
Fig.3 (a) Schematic diagram of a redox flow sodium-ion battery based on redox-targeting reaction[45]; (b) Schematic diagram of redox-targeting vanadium flow battery (RT-VRB)[58]; (c) Schematic diagram of the structure and operation of a redox mediated zinc air fuel cell (RM-ZAFC)[69]; (d) Schematic diagram of solar rechargeable batteries based on redox-targeting reaction[70]
Fig.4 (a) An electrochemical approach based on a double-layer electrode to determine the reaction kinetics[82]; (b) FTIR spectra of standard PB and BG, Br2-oxidized PB, and Br--reduced BG[66]; (c) Fe 2p XPS spectra of PB and Br2-oxidized PB[66]; (d) XRD patterns of NVP collected from the catholyte tank before and after charging[45]; (e) ND patterns of pristine and partially reduced PB by [Fe(CN)6]4-[66]; (f) The most probable structures of pristine (bottom) and reduced PB (or PW, top) unit cells obtained from the refinement of ND patterns[66]
Fig.5 (a) Interfacial charge-transfer kinetics of redox-targeting reactions measured by SECM[83]; (b) In situ UV-Vis spectra of DHPS electrolyte before and after addition of excess zinc[84]; (c) Operando ATR-FTIR spectra of DHPS electrolyte recorded during resting, after adding excess zinc and during discharge process[84]; (d) Fluorescence microscopic images of a planar quartz reactor filled with 20 mmol/L fully reduced FL upon reacting with a compact NVP granule assembly[45]
Fig.6 (a) Utilization of LiFePO4 as a function of power in an SMRT system and correlation of power and energy at different utilizations of solid material[9]; (b) lgieffn- η relationship (including polarization curve)[84]; (c) Kinetic data of SMRT reaction in NVP/MPTZ system[45];(d) Oxidation kinetics of LFP30 oxidized by [Fe(CN)6]3- [85]
Fig.7 (a) An energy-storage tank filled with active materials[10]; (b) Photograph of a bottle filled with LiFePO4 processed into granules[9]; (c) Adsorption column to remove a substance[88]; (d) The utility model relates to a sewage treatment device[89]; (e) Outlook for future study of redox-targeting flow battery energy storage technology
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