Zheng Li’s research while affiliated with Massachusetts Institute of Technology and other places
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Batteries which use dissolved redox-active species, such as redox flow batteries (RFBs), are often considered to be constrained in their operation and energy density by the solubility limit of the redox species. Here, we show that soluble redox active electrolytes can be reversibly cycled deeply into the precipitation regime, permitting higher effective concentrations, higher energy densities, and lower costs. Using aqueous sodium polysulfide negative electrolytes cycled in the nominal Na2S2 to Na2S4 capacity range as an example, we show that the effective solubility can be increased from 5M in the fully-dissolved state to as much as 10M using the precipitation strategy. Stable cycling was observed at 8M concentration over more than 1600h at room temperature. We also analyze the range of polysulfide electrochemical stability, and characterize the precipitate composition before and after aging. This enhanced effective concentration approach may be generalized to other redox chemistries that utilize solubilized reactants, and may be especially useful for long-duration storage applications where slow charge-discharge rates allow equilibration of precipitated species with the redox-active solution.
The intermittency of renewable electricity generation has created a pressing global need for low-cost, highly scalable energy storage. Although pumped hydroelectric storage (PHS) and underground compressed air energy storage (CAES) have the lowest costs today (∼US1/kWh when using sodium polysulfide. The projected storage economics parallel those for PHS and CAES but can be realized at higher energy density and with minimal locational constraints.
In this Backstory, Yet-Ming Chiang and colleagues explain how their cost-focused approach led to the discovery of an affordable battery technology based on readily available materials. Their findings appear in the October 2017 issue of Joule.
Sulfur is an attractive reactant for such concepts due to its exceptionally low cost, high natural abundance, and high specific and volumetric capacity owing to its two-electron reaction. Taking the cost-per-capacity (e.g., in US/kWh). Results of techno-economic modeling are also presented, which show that when projected to full system-level, this new approach has energy and power costs that are comparable to those of pumped hydroelectric storage (PHS) and underground compressed air energy storage (CAES), but without their geographical and environmental constraints.
This work was supported as part of the Joint Center for Energy Storage Research, an Energy Innovation Hub funded by the U.S. Department of Energy, Office of Science, Basic Energy Sciences.
Virtually all intercalation compounds exhibit significant changes in unit cell volume as the working ion concentration varies. NaxFePO4 (0<x<1, NFP) olivine, of interest as a cathode for sodium-ion batteries, is a model for topotactic, high strain systems as it exhibits one of the largest discontinuous volume changes (~17% by volume) during its first-order transition between two otherwise isostructural phases. Using synchrotron radiation powder X-ray diffraction (PXD) and pair distribution function (PDF) analysis, we discover a new strain-accommodation mechanism wherein an amorphous phase forms to buffer the large lattice mismatch between primary phases. While the new phase has short-range order only, it is refined with a periodicity closing matching the a and b lattice parameters of one crystalline endmember phase, and the c lattice parameter of the other. Within this amorphous phase form very fine spherical nanocrystallites of the olivine phase. We suggest that amorphous phase formation is a strain-accommodation mechanism that may apply to systems with large transformation strains.
Redox flow batteries have the potential to provide low-cost energy storage to enable renewable energy technologies such as wind and solar to overcome their inherent intermittency and to improve the efficiency of electric grids. Conventional flow batteries are complex electromechanical systems designed to simultaneously control flow of redox active fluids and perform electrochemical functions. With the advent of redox active fluids with high capacity density, i.e., Faradaic capacity significantly exceeding the 1–2 M concentration equivalents typical of aqueous redox flow batteries, new flow battery designs become of interest. Here, we design and demonstrate a proof-of-concept prototype for a “gravity-induced flow cell” (GIFcell), representing one of a family of approaches to simpler, more robust, passively driven, lower-cost flow battery architectures. Such designs are particularly appropriate for semi-solid electrodes comprising suspensions of networked conductors and/or electroactive particles, due to their low energy dissipation during flow. Accordingly, we demonstrate the GIFcell using nonaqueous lithium polysulfide solutions containing a nanoscale carbon network in a half-flow-cell configuration and achieve round trip energy efficiency as high as 91%.
In this work we investigated an energy-efficient bio-templated route to synthesize nano-structured FePO4 for sodium-based batteries. Self-assembled M13 viruses and single wall carbon nanotubes (SWCNTs) have been used as a template to grow amorphous FePO4 nanoparticles at room temperature (the active composite is denoted as Bio-FePO4-CNT) to enhance the electronic conductivity of the active material. Preliminary tests demonstrate a discharge capacity as high as 166 mAh/g at C/10 rate, corresponding to composition Na0.9FePO4, which along with higher C-rate tests show this material to have the highest capacity and power performance reported for amorphous FePO4 electrodes to date.
Electroanalytical, structural, and microanalytical techniques are combined to demonstrate the first clear and convincing case of electrochemical storage by Al-ion intercalation in a Prussian blue analog host. In addition, a high power asymmetric capacitor using Al-ion intercalation is demonstrated. Al, Fe, and Cu elemental maps of intercalated Al0.18 K0.02Cu[Fe(CN)6]0.7·3.7H2O obtained by transmission electron microscopy (TEM) energy-dispersive X-ray spectroscopy (EDX) area scan are shown.
We recently demonstrated that the high solubility of polysulfides in nonaqueous electrolytes can be exploited to make a high energy density lithium-sulfur flow battery with low storage cost 1–3 . Here we used a new approach, whereby percolating networks of nanoscale conductor particles (in this case carbon black) are incorporated within the electrode forming an embedded current collector which distributes electrochemical activity throughout the volume of the flow electrode, rather than being confined to the surfaces of stationary current collectors. Compared to the traditional approach, this architecture enables significantly higher capacity (~1200 mAh / g S) and reversibility by allowing cycling of polysulfide solutions (2.0-2.5V) into the precipitation regime (~2V), where discharge proceeds via precipitation of insoluble Li 2 S, as shown in Figure 1.
The majority of the available capacity of this battery lies in this precipitation regime. Therefore, understanding the kinetics of the precipitation process is essential to improving the reversibility and rate capability of lithium-sulfur flow batteries. Here, we will discuss the nucleation and growth kinetics of the precipitates on various conductive substrates, including various carbon surfaces and conducting oxides. Moreover, we will discuss the effects of cycling conditions and substrate on the morphology of the precipitates, examples of which are shown in Figure 2. The precipitation of lithium sulfide has long been a challenge for lithium-sulfur batteries due to its low electronic conductivity 4,5 , so controlling the morphology of precipitates can reduce losses due to Ohmic polarization.
For a given depth of discharge, higher electrode level energy densities (Wh/L) may be obtained by increasing the sulfur concentration in the polysulfide solution. However, as sulfur concentration—and therefore electrode capacity—increase, the current needed to cycle at a fixed C-Rate increases as well. Therefore, it is important to understand the concentration-dependent transport and kinetic properties of lithium polysulfide solutions so that the rate-limiting mechanisms may be appropriately addressed. We have undertaken a systematic effort to characterize the ionic conductivity and exchange current density of lithium polysulfide solutions in various solvents as a function of sulfur concentration and solution composition (i.e. n in Li 2 S n ). Figure 3 shows the concentration-dependent ionic conductivity of Li 2 S 8 solutions in selected non-aqueous solvents.
Acknowledgements:
This work was supported as part of the Joint Center for Energy Storage Research, an Energy Innovation Hub funded by the U.S. Department of Energy, Office of Science, Basic Energy Sciences.
Figure captions:
Figure 1. Fivefold higher reversible capacity for the nanoscale conductor suspension (1.5 vol% carbon black) compared to a traditional carbon fiber current collector when galvanostatically cycling in a non-flowing cell with a lithium anode.
Figure 2. Scanning electron microscope image of lithium sulfide precipitates on a network of multi-walled carbon nanotubes after first discharge of a stationary lithium polysulfide cell at C/4 rate. On the circled nanotube, lithium sulfide particles merge together to form a conformal coating.
Figure 3. Ionic conductivity of lithium polysulfide solutions (Li 2 S 8 ) in selected nonaqueous solvents at varying sulfur concentrations from 1-8M.
1. Fan, F. Y. et al. Polysulfide Flow Batteries Enabled by Percolating Nanoscale Conductor Networks. Nano Lett. (2014). doi:10.1021/nl500740t
2. Demir-Cakan, R. et al. Li--S batteries: simple approaches for superior performance. Energy {&} Environ. Sci. 6, 176 (2012).
3. Yang, Y., Zheng, G. & Cui, Y. A membrane-free lithium/polysulfide semi-liquid battery for large-scale energy storage. Energy {&} Environ. Sci. 6, 1552 (2013).
4. Bruce, P. G., Freunberger, S. A., Hardwick, L. J. & Tarascon, J.-M. Li – O 2 and Li – S batteries with high energy storage. Nat. Mater. 11, 19–30 (2012).
5. Manthiram, A., Fu, Y. & Su, Y.-S. Challenges and prospects of lithium--sulfur batteries. Acc. Chem. Res. 46, 1125–1134 (2013).
Citations (13)
... [5] Recently, sulfur-based aqueous batteries (SABs), featuring a high theoretical capacity (1672 mAh g s À 1 ), low cost and abundant resources, have garnered ever-increasing attention. [6][7][8][9][10][11][12][13][14][15][16][17][18][19] Nevertheless, the practical deployment of SABs faces challenges related to the sulfur cathode, including severe polysulfide dissolution and sluggish conversion reaction kinetics during the solid-liquid (S-L) sulfur redox process, leading to continuous active material loss and low Coulombic efficiency. [20][21] Up to now, tremendous efforts have been devoted to addressing the challenges in SABs. ...
... NaSICON has a wide electrochemical stability window that permits a wide variety of catholyte and anolyte chemistries. For instance, Li et al. 140 utilized air as catholytes and sulfides as anolytes to fabricate an RFB cell that can operate with a cell voltage of 1.68 V in acidic condition or 0.85 V in alkaline condition. Allcorn et al. 104 illustrated the utilization of NaSICON membrane in an aqueous neutral pH RFB, employing Fe-bpy as the catholyte and Fe-EDTA as the anolyte at room temperature. ...
... The cost of PHS investment, as per the calculations, ranges from 190 to 350e per kilowatt-hour. In Fig. 26, NaS batteries cost between 1000 and 3000 USD/kW, according to [215], while Li-ion batteries cost between 175 and 4000 USD/kW, with NaS batteries being the most expensive. For the most recent data, NaS batteries cost between 350 and 440 e per kWh, while Li-ion batteries cost between 700 and 1400 e per kWh. ...
... The current research on the structure of LFMP mainly focuses on the structural evolution of Mn and Fe redox reactions, lithiation reaction kinetics, and the impact of lattice defects on performance during the charge-discharge process [10,[38][39][40] . These mechanistic studies provide important clues for developing higherperformance LIBs and investigating the degradation mechanisms of these batteries [24,30] . ...
... Received 8 March 2024; Received in revised form 2 May 2024; Accepted 9 May 2024 model, wherein the electrolytes inside the tanks are assumed to remain uniformly mixed, instantaneously adjusting their State of Charge (SoC) across the entire tank volumes during charge and discharge processes [8,9]. The studies on tanks have primarily centered on rebalancing strategies [10,11] to rectify tank imbalance side effects, for which different strategies have been proposed with the aim of restoring the initial performance of the battery [12,13]. ...
... Due to the fact that the electrode design requirements of SIBs are similar to those of LIBs, the peptide-mediated synthesis can be beneficially explored. To explore the cathode materials for SIBs, Moradi et al. [ 15 ] demonstrated an energy-efficient bio-templated route to synthesize nanostructured FePO as the electrode material, in which self-assembled M13 viruses and singlewalled carbon nanotubes (CNTs) were used as the templates to grow amorphous FePO nanoparticles, so as to improve the electronic conductivity of the active material. Experimental tests confirmed the high discharge capacity of 166 mAh/g at C/10 rate, along with higher C-rate tests verifying the as-prepared material have the best capacity and power performance compared to reported FePO electrodes. ...
... Figure 4b is a high-resolution map of C 1 s, with four fitted peaks located at 283.8, 285.7, 286.8, and 88.6 eV. These peaks correspond to C=C/C-C [24], C-N [25], C-S/C-O [26,27], and C-F [16], respectively. ...
... Their large interstitial sites and diffusion tunnels can facilitate the intercalation/de-intercalation of Al 3+ . 96 In 2015, Liu et al. first applied PBAs as cathodes of AABs (Fig. 12a). 97 In a three-electrode electrochemical system, copper hexacyanoferrate (KCu[Fe(CN) 6 ]·8H 2 O, CuHCF) prepared via the co-precipitation strategy exhibited a capacity of 46.9 mA h g −1 at 40 mA g −1 with a retention of 54.9% over 100 cycles in 0.5 M Al 2 (SO 4 ) 3 (Fig. 12b). ...
... In addition, its economical and environmentally friendly characteristics have shown potential for large-scale energy systems. 1 To date, various ARBs based on other metal ion charge carriers, such as Na + , K + , Mg 2+ , Ca 2+ , Zn 2+ , and Al 3+ , have been widely developed. [2][3][4][5][6][7][8][9] Compared with metal ions, aqueous ammonium ion batteries (AAIBs) with non-metallic ions (NH 4 + ) as charge carriers have garnered particular attention due to their particular energy storage mechanism. Specifically, the light molar mass (18 g mol −1 ) and small hydrated ionic size (3.31 ...
... Hence, the charge density flux J is constant at every position inside the domain. With time evolving, the composition c changes the material-dependent conductivity σ(c), as reported in Ref. 47 for the Li 4x+3 Ti5O 12 phase. Hence, the charge density flux J is also modified. ...