Patent Publication Number: US-10770699-B2

Title: Stable bromine charge storage in porous carbon electrodes using tetraalkylammonium bromides for reversible solid complexation

Description:
CROSS REFERENCE TO RELATED APPLICATIONS 
     This application is a continuation-in-part under 35 U.S.C. § 120 and § 365(c) of co-pending U.S. Utility patent application Ser. No. 14/692,695, filed Apr. 21, 2015, by Galen D. Stucky, Brian Evanko, Nicholas Parker, David Vonlanthen, David Auston, Shannon Boettcher, Sangeun Chun, Xiulei Ji, Bao Wang, Xingfeng Wang and Raghu Subash Chandrabose, entitled “ENERGY STORAGE DEVICE INCLUDING REDOX-ENHANCED ELECTROLYTE,” (UC Ref 2014-716), which application claims the benefit under 35 U.S.C. Section 119(e) of U.S. Provisional Patent Application No. 61/982,236, filed May 21, 2014, by Galen D. Stucky, Brian Evanko, Shannon Boettcher, Sangeun Chun, Xiulei Ji, and Bao Wang, entitled “HIGH VOLTAGE REDOX ELECTROLYTES FOR ENHANCED ELECTROCHEMICAL CAPACITOR PERFORMANCE AND REDUCED SELF-DISCHARGE,” Attorney&#39;s Docket No. 30794.548-US-P1 (2014-716); 
     all of which applications are incorporated by reference herein. 
    
    
     STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH AND DEVELOPMENT 
     This invention was made with Government support under Grant No. DE-AR0000344, awarded by the U.S. Department of Energy (DOE). The Government has certain rights in this invention. 
    
    
     BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     This invention relates to energy storage devices. 
     2. Description of the Related Art 
     (Note: This application references a number of different references as indicated throughout the specification by one or more reference numbers in superscripts, e.g.,  x . A list of these different references ordered according to these reference numbers can be found below in the section entitled “References.” Each of these references is incorporated by reference herein.) 
     Electric double-layer capacitors (EDLCs), interchangeably referred to as supercapacitors or ultracapacitors, are capable of storing and discharging energy quickly due to a physical ion adsorption/desorption mechanism in the Helmholtz layer. 1,2  Compared to EDLCs using non-aqueous electrolytes, EDLCs with nonflammable aqueous electrolytes are in principle safer, and provide higher power density due to their having a lower ionic resistance. 1,3-5  However, the energy density of aqueous EDLCs is limited by the narrow electrochemical potential window of water compared to counterparts with organic electrolytes or ionic liquids. 6-8  The grand challenge for aqueous EDLCs is to increase specific energy without compromising specific power and cycling stability. A number of hybrid and pseudocapacitive systems have been developed that utilize different charge storage mechanisms in addition to, and/or in place of, electric double-layer capacitance to increase energy density. 9-15    
     One such approach to enhance the energy density is to replace the inert electrolytes of conventional EDLCs with redox-active electrolytes that enable faradaic charge storage. 16-23  High-energy redox electrochemical capacitors (ECs) must concurrently utilize a catholyte and an anolyte (dual-redox enhanced electrochemical capacitors; dual-redox ECs) to maximize faradaic energy storage. 19,23,25,26,36  Compared with the construction of nanostructured solid-state redox-active electrode materials, liquid-state redox-active electrolytes are easier to prepare and be scaled up, and should be compatible with the carbon electrodes that are currently mass-produced for commercial EDLCs. 
     In order to design redox-active electrolyte systems, redox couples should exhibit fast and reversible electron transfer and not engage in irreversible side reactions and/or degradation over repeated charge/discharge cycles. Additionally, the cross-diffusion of soluble redox couples that causes low Coulombic efficiency and fast self-discharge must be eliminated. The use of ion-selective membrane separators to mitigate self-discharge has been reported, 24  but such membranes are costly, and primarily for that reason are not practical for commercial applications. Electrostatic attraction has also been proposed as a mechanism to retain redox couples at the surface of oppositely charged electrodes, but was shown to have only a minor effect on the suppression of self-discharge rates. 25,26    
     Halogens (I −  and Br − ) are promising aqueous redox-active species as they are inexpensive, electrochemically reversible redox couples with high solubility. 22,25,27-31  In comparison to iodide, bromide has a higher standard reduction potential (0.81 V vs SCE; E I     3       −     /I     −     o =0.3 V) that further increases energy density. However, this advantage is offset by the corrosive and volatile nature of bromine generated at the positive electrode. Furthermore, soluble Br 3   −  diffuses to the negative electrode, which causes low Coulombic efficiency and fast self-discharge, as well as possible irreversible oxidation or bromination of the anode or anolyte. 32,33  In aqueous bromine flow batteries, asymmetric quaternary ammonium salts such as methyl ethyl pyrrolidinium bromide (MEPBr; 1-ethyl-1-methylpyrrolidinium bromide) or methyl ethyl morpholinium bromide (MEMBr; 4-ethyl-4-methylmorpholinium bromide) are commonly used to complex Br 2 /Br 3   −  as an oily-liquid phase. 34,35  This complexation reduces the reactivity and vapor pressure of bromine while maintaining a mobile, liquid state for flow-system compatibility. However, this approach does not address the cross-diffusion and poor Coulombic efficiency. 32  Standard bromine flow batteries avoid these limitations by storing the charged liquid complex in a separate tank away from the cell stack, but this practice is not feasible for non-flow systems, such as in redox-enhanced electrochemical capacitors (redox ECs). Alternatively, ion-exchange membrane separators can be used, but these materials are expensive and require addressing significant sealing challenges to be effective in a practical device. In short, a fundamental need is to store Br 3   −  in non-flow energy storage systems in a manner that (1) reduces the unwanted chemical reactivity and vapor pressure of bromine but at the same time (2) suppresses cross-diffusion and self-discharge by (3) a simple and affordable mechanism. Embodiments of the present invention satisfy this need. 
     SUMMARY OF THE INVENTION 
     The present disclosure reports on surprising and unexpected uses of viologen, tetraalkylammonium, and/or zinc in electrolytes for EDLCs. 
     In a first embodiment, the electrolyte includes a first redox couple comprising bromine and a second redox couple comprising a viologen. During charging, the electrolyte evolves into a catholyte including the first redox couple and an anolyte including the second redox couple. When charged, the charge is stored in faradaic reactions with the first and second redox couples in the electrolyte and in a double-layer capacitance of a porous carbon material that comprises at least one of the electrodes. 
     In various embodiments, the viologen has the structure: 
     
       
         
         
             
             
         
       
     
     wherein R is an alkyl. Examples of the viologen anolyte include, but are not limited to, ethyl viologen, butyl viologen, pentyl viologen, hexyl viologen, and other viologens. It is preferable that the alkyl comprises at least 4 carbon atoms, in order to strongly adsorb to the carbon electrode when reduced. 
     In yet further embodiments, the catholyte also comprises a viologen. The viologen in the catholyte may be the same as, or different from, the viologen in the anolyte. Examples of the viologen in catholyte include, but are not limited to, hexyl viologen and pentyl viologen. In one or more examples, the viologen in the catholyte is a complexing agent that forms a complex with the bromine. 
     The present disclosure further describes, for the first time, tetrabutylammonium-induced, reversible solid complexation of the Br − /Br 3   −  redox couple in aqueous redox ECs. Systematic studies show that this solid complex is retained in the pores of the high-surface-area carbon electrodes (without the use of an expensive ion-selective membrane to separate cell compartments) upon charging, suppressing cross-diffusion and preventing unwanted chemical reactivity that would cause electrode degradation, and thereby dramatically improving cycling stability and self-discharge relative to traditional oily-liquid-phase bromine complex. Furthermore, the present disclosure reveals the underlying cause of the irreversible capacity loss that occurs when the uncomplexed Br − /Br 3   −  redox couple is used in aqueous redox ECs with activated carbon electrodes. 
     Building upon these findings, a high-performance and stable aqueous redox EC was designed. The compatibility and comparative Br 3   −  complexing capacity was investigated to demonstrate the utility of bromide catholyte and the complexation strategy in such a system. In one illustrative embodiment, the use of readily available tetrabutylammonium bromide as an additive, and a dual-redox EC that utilizes bromide and a highly soluble ethyl viologen (EV) as an anolyte, produced a specific energy of ˜64 W·h/kg (at 1 A/g and normalized to the dry mass of both positive and negative electrode), representing a ˜230% improvement over commercial non-aqueous electric double-layer capacitors. In addition, the EC comprising tetrabutylammonium bromide as an additive maintains stability over 7000 cycles. 
     In yet a further embodiment, the electrolyte includes any tetraalkylammonium bromide as described herein forming a solid complex with bromine. In yet a further embodiment, the second redox couple comprises zinc. In various implementations using zinc, the electrolyte does not need to include a viologen. Such an electrolyte may be used in supercapacitors or supercapacitor/battery hybrids. 
     In one or more embodiments wherein the electrolyte comprises a zinc halide, the energy storage device, comprises a cathode and an anode in contact with an electrolyte including zinc halide; and tetraalkylammonium complexing agent (e.g., tetrabutylammonium bromide or cetyltrimethylammonium bromide) on the cathode. During charging, the zinc from the zinc halide plates onto the anode and the halogen in the halide oxidizes so as to form a solid complex with the tetraalkylammonium on the cathode. 
     The present disclosure further describes an energy storage device comprising a pouch having a first wall and a second wall, the first wall and the second wall each including a thin (&lt;100 μm) flexible current collector comprising an electrically conductive carbon-polymer composite. The device further comprises an electrically insulating plastic spacer, one or two electrodes, an electrolyte, and a separator inside the pouch; and a heat seal to join the first wall, second wall, and the plastic spacer, so that the electrode(s), the electrolyte, and the separator are sealed inside the pouch. 
     Typically, the plastic spacer is between the first wall and the second wall. The electrodes are on either side of the separator, between the separator and the walls. If there is only one electrode then one side of the separator is in direct contact with a wall. The electrolyte is between the first wall and the second wall, permeating the electrode(s) and separator. The carbon-polymer composite pouch cell is corrosion resistant, providing an alternative to metal current collectors that is compatible with corrosive aqueous electrolytes. 
     In one or more embodiments, multiple cells are stacked on top of one another in a series configuration to get higher voltages. In such an arrangement, the positive current collector of one cell and the negative current collector of the adjacent cell can be replaced by a single bipolar current collector made of the carbon-polymer composite. The bipolar pouch cell provides a practical method for implementing (e.g., large) supercapacitor/EDLC cells based on (1) a viologen bromide system (wherein viologen is used at the anode and cathode), (2) tetraalkylammonium solid complexation of bromine in activated carbon (wherein viologen is at the anode, tetraalkylammonium is at the cathode along with bromide), or zinc bromide/tetraalkylammonium systems (wherein zinc is at the anode, tetraalkylammonium and bromide are at the cathode). 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       Referring now to the drawings in which like reference numbers represent corresponding parts throughout: 
         FIG. 1  illustrates an energy storage device during charging, in accordance with at least one example. 
         FIG. 2  illustrates an energy storage device during discharging, in accordance with at least one example. 
         FIG. 3( a )  plots UV-Vis of MV and HV with chemically generated Br 3   − . For ease of comparison, the observed absorbance is normalized;  FIG. 3( b )  is a visual comparison of MV and HV complex formation with chemically generated Br 3   − . 
         FIG. 4  plots galvanostatic charge/discharge cycling with MVCl 2  and NaBr. 
         FIG. 5( a )  illustrates synthesis of viologens and  FIG. 5( b )  plots cyclic voltammetry of each viologen. 
         FIG. 6  plots UV-Vis with viologens and chemically generated Br 3   −  (20 mM of viologen and 40 mM of Br 3   − . 
         FIGS. 7( a )-7( c )  plot the galvanostatic charge/discharge profiles (dashed green lines) of the PV/Br redox couples for cell testing up to 1.15 V ( FIG. 7( a ) ), 1.2 V ( FIG. 7( b ) ), and 1.25 V ( FIG. 7( c ) ); the positive electrode (solid blue) and the negative electrode (solid red), respectively, are referenced to the centrally placed SCE. 
         FIG. 8  shows competitive Br 3   −  complexing ability of quarternary ammonium salts (MEP, TPA, and TBA) with MV, PV, and HV. 
         FIGS. 9( a )-9( c )  plot the galvanostatic charge/discharge potential profiles of the asymmetric cells (blue curves) divided into contributions from the positive electrode (orange curves) and the negative electrode (purple curves), referenced to the centrally placed Ag/AgCl reference electrode. The cells were charged/discharged at a rate of 2 A/g (based on the mass of positive electrode only) to 1 V, with a 4:1 negative to positive electrode mass ratio; the aqueous electrolytes were 1.2 M KBr ( FIG. 9( a ) , 1 M KBr+0.2 M MEPBr ( FIG. 9( b ) ), and 1 M KBr+0.2 M TBABr ( FIG. 9( c ) ). 
         FIG. 10( a )  shows complexation of chemically generated Br 3   −  by the addition of potassium bromide (left), MEPBr (middle), and TBABr (right). 
         FIG. 10( b )  shows an electrochemically generated [TBA + .Br 3   − ] solid complex by controlled potential electrolysis. 
         FIG. 10( c )  shows Raman spectra of the electrochemically generated [TBA + .Br 3   − ] solid complex (blue curve) and commercial [TBA + .Br 3   − ] solid complex (orange curve). 
         FIGS. 11( a )-11( b )  show scanning transmission electron microscopy (STEM) images of electrolyzed C pellet ( FIG. 10( a ) ) and the control C pellet ( FIG. 10( b ) ), collected by a high-angle annular dark-field (HAADF) detector. Sample preparation steps including controlled potential electrolysis are detailed in the experimental section. 
         FIGS. 12( a )-12( d )  plot performance of two-electrode asymmetric cells constructed with aqueous electrolytes of 1.2 M KBr (blue curve), 1 M KBr/0.2 M MEPBr (black curve), and 1 M KBr/0.2 M TBABr (orange curve), respectively, the cells were charged/discharged at a rate of 2 A/g (based on the mass of positive electrode only) to 1 V, with a 4:1 negative to positive electrode mass ratio,  FIG. 12( a )  plots cycling stability of each cell tested at 25° C.; the inset shows two-electrode potential profiles vs capacity,  FIG. 12( b )  plots open circuit (OC) energy efficiency (η R ) for each cell at 25° C. Each data point was collected by charging the cell, allowing it to sit at open circuit for 2, 6, or 10 h, then discharging the cell completely. For the KBr electrolyte, self-discharge was tested for both a 1 V charge (solid blue) and a 1.2 V charge (dashed blue),  FIG. 12( c )  plots cycling stability of each cell tested at 40° C., and  FIG. 12( d )  plots η R  at a given time for each cell at 40° C. 
         FIG. 13( a )  plots Raman spectra of the separators after cycling, wherein Raman peaks for the non-cycled carbon electrode (green curve) are added to the plot for the comparison. 
         FIGS. 13( b )-13( e )  are SEM images of positive electrodes, before cycling ( FIG. 13( b ) , of an electrode from a KBr cell after cycling ( FIG. 13( c ) ), of an electrode from a KBr/TBABr cell after cycling ( FIG. 13( d ) ), and of an electrode from a KBr/MEPBr cell after cycling ( FIG. 13( e ) ), 
         FIGS. 14( a )-14( b )  plot performance of 1.2 M EVBr 2 /3 M NaBr cells, wherein  FIG. 14( a )  plots three-electrode GCD potential profiles for the positive electrode (orange curve), negative electrode (purple curve), and total cell (blue curve) cycled to 1.35 V at 1 A/g, during charging, the electrochemical behavior transitions from capacitive to faradaic at both electrodes, and  FIG. 14( b )  plots specific energy, cycling stability and Coulombic efficiency of an EV/Br two-electrode cell cycled to 1.35 V at 1 A/g. 
         FIG. 15  plots UV-vis absorption spectra quantifying the concentration of EV 2+  remaining dissolved in the supernatant without Br 3   −  (EV 2+ ; blue open-square curve), with the addition of Br 3   −  (EV 2+ /Br 3   − ; blue open-circle curve), with Br 3   −  and TBABr (EV 2+ /Br 3   − /TBA + ; orange solid curve), and with Br 3   −  and MEPBr (EV 2+ /Br 3   − /MEP + ; black solid curve), respectively, wherein the spectra are normalized to the absorption maxima of the EV 2+  (λ max =260 nm) (experimental details for the UV-vis measurements are in the experimental section). 
         FIGS. 16( a )-16( d )  plot performance of a 1.2 M EVBr 2 /0.12 M TBABr/2.88 M NaBr cell, wherein  FIG. 16( a )  plots specific energy and cycling stability of EV/Br cells with and without TBABr (the inset shows GCD profiles at the 1000 th  cycle),  FIG. 16( b )  plots long-term cycling stability of the EV/TBA/Br cell cycled at 2 A/g to 1.3 V, and to 1.35 V (the inset shows GCD profiles for the last 3 cycles),  FIG. 16( c )  plots open circuit voltage for 6 h after charging the cell to 1.35 V (orange curve) and 1.3 V (blue curve), respectively, and  FIG. 16( d )  plots specific energy vs power of the EV/TBA/Br cell (orange curve) and its comparison to Na 2 SO 4  (black curve) and commercial Maxwell (green curve) cells. Specific energy and power of all cells, including the commercial EDLC, were normalized to the dry mass of both positive and negative electrodes. Rate tests of the EV/TBA/Br cell were performed after the initial 1000 GCD cycles at 1 A/g. 
         FIG. 17  illustrates a contact angle of test electrolyte on the surface of a porous activated carbon pellet, showing (left) aqueous KBr solution droplet, (middle) aqueous MEPBr solution droplet, and (right) aqueous TBABr solution droplet. 
         FIG. 18( a )  is a cyclic voltammogram of 1 M KBr/0.2 M TBABr for a scan rate of 10 mV/s, wherein an activated carbon pellet pasted on the carbon cloth served as working electrode and a Pt wire as counter electrode (as reference, an Ag/AgCl electrode was used). 
         FIG. 18( b )  shows schematic illustration of stable bromine charge storage in porous carbon electrodes. 
         FIG. 19  shows electrochemical generation of a [TBA + .Br 3   − ] solid complex. Controlled potential electrolysis with 1 M KBr/0.2 M TBABr solution was performed with a non-porous graphite rod as working electrode, a Pt wire as the counter electrode, and an Ag/AgCl reference electrode. 
         FIG. 20  shows separators (Whatman™ #1 filter paper) after GCD cycling, showing (left) a separator from an asymmetric KBr/TBABr cell; (middle) separator from an asymmetric KBr/MEPBr cell; and (right) separator from asymmetric KBr cell. 
         FIG. 21( a )  is a transmission electron microscope (TEM) image showing the positive electrode before cycling (for comparison) and  FIGS. 21( b )-21( d )  are TEM images of the positive electrodes after GCD cycling, for an electrode from a KBr cell ( FIG. 12( b ) ), an electrode from a KBr/TBABr cell ( FIG. 21( c ) , and an electrode from KBr/MEPBr cell ( FIG. 21( d ) ). 
         FIGS. 22( a )-22( c )  are cyclic voltammograms of 0.1 M EVBr 2  ( FIG. 22( a ) ) and 0.1 M EVBr 2 /0.1 M NaBr ( FIGS. 22( b ) and 22( c ) , wherein the data in  FIG. 22( b )  was obtained by scanning from 0 V to −0.95 V (purple curve) and 0 V to +1.1 V (orange curve), separately, and the data in  FIG. 22( c )  was obtained by scanning over the full range of +1.1 V to −0.95 V (scan rate: 20 mV/s); glassy carbon served as the working electrode and a Pt wire served as the counter electrode. As reference, an Ag/AgCl electrode was used. 
         FIG. 23( a )  plots galvanostatic cycling of a PV/TBABr/NaBr cell with a whatman separator (charged/discharged at a rate of 1 A/g). 
         FIG. 23( b )  is a summary of the viologen bromide system, illustrating a single electrolyte is used with a non-ion-selective separator, where anolyte and catholyte are fully mixed and fully compatible. By optimizing the functional group, a solid complex is reversibly electroprecipitated at each electrode to improve cycling stability and decrease self-discharge. The redox couples come from a single organic salt that dissociates into anionic and cationic species, each of which acts as a charge-storing redox couple at one electrode and as a complexing agent at the other electrode. 
         FIGS. 23( c )-23( f )  plot performance of a 1 M PVBr 2 /3 M NaBr cells, showing, in  FIG. 23 ( c )  GCD potential profiles for the cathode (red curve), anode (blue curve), and total cell (green curve),  FIG. 23( d )  specific energy of PV/Br and HV/Br cells at different discharge rates,  FIG. 23 ( e )  energy retention is 97% over 10,000 cycles at 2.5 A/g dry  with 99.9% coulombic efficiency, and  FIG. 23( f )  stable cycling with the leads switched every 200 cycles, repeatedly reversing the polarity. Additionally these cells retain more than 75% of initial discharge energy after 6 hours at open circuit. 
         FIG. 24  shows a bipolar pouch cell design for n cells in series. 
         FIGS. 25( a )-25( d )  show a pouch cell with carbon black-impregnated polyethylene (CB-PE) current collectors. The current collectors are separated by non-conducting polyethylene and the edges of the cell are heat-sealed. 
         FIG. 26  shows galvanostatic cycling profiles at 1 A/g dry  for a cell with 3 M NaBr/0.85 M PVBr 2  electrolyte in a glassy carbon Swagelok cell and in a PE-CB pouch cell. 
         FIG. 27  plots cycling stability for the PE-CB pouch cell with 0.85 M PVBr 2 /0.1 M TBABr/3 M NaBr electrolyte cycled at 1 A/g dry  to 1.25 V. 
         FIGS. 28( a )-28( d )  are schematics for a bipolar pouch cell ( FIG. 28( a ) ) with CB-PE composite current collectors and the concept reduced to practice with large square electrodes instead of a small circular stack ( FIG. 28( b ) . 
         FIGS. 29( a )-29( b )  plot specific charge/discharge energy and Coulombic efficiency normalized to electrode mass ( FIG. 29( a ) ) and typical galvanostatic charge/discharge potential profile ( FIG. 29( b ) ) for a PE-CB pouch cell with 1 M PVBr 2 /0.1 M TBABr/3 M NaBr electrolyte cycled at 0.5 A/g dry  to 4.8 V. 
         FIGS. 30( a )-30( f )  show example cross sections of different pouch cell geometries. 
         FIG. 31  illustrates zinc bromine redox-EC cell construction. The activated carbon is pre-soaked in a TBABr solution to pre-adsorb complexing agent at the surface. Then the electrode is contacted with a zinc bromide electrolyte and assembled into a cell with a paper separator. 
         FIG. 32  illustrates the zinc bromine redox EC mechanism. With this chemistry, zinc is reversibly plated at the negative electrode and bromide is reversibly oxidized to tribromide and complexed into an insoluble solid with TBA +  at the positive electrode. 
         FIG. 33  illustrates self-discharge with and without TBABr. The fraction of the initial discharge energy retained after different periods at open circuit is much higher for cells with TBA complexing agent than for equivalent cells with no complexing agent. 
         FIG. 34  illustrates typical galvanostatic potential profile for a ZnBr 2  cell. In this cell, the positive electrode is pre-soaked in 0.25 M TBABr and then both the separator and electrode are saturated with electrolyte containing 2.5 M ZnBr 2 , 0.5 M NaBr, and 1 wt. % PEG 200 . The cell charges to nearly 1.8 V at 1 A/g before cutoff at 150 mAh/g. The resulting charge/discharge plateaus are very flat, characteristic of the zinc bromine cell chemistry. 
         FIG. 35  shows discharge rate tests. Heptyl viologen, pentyl viologen, and zinc bromine cells are charged at 10 mA/cm 2  and discharged at different rates. Specific energy is normalized to the dry mass of the activated carbon electrode(s). 
         FIG. 36  shows a discharge Ragone Plot. Specific energy and power are normalized to the mass of the activated carbon electrodes and electrolyte for viologen cells and to the mass of the activated carbon electrode, separator, and electrolyte for the zinc bromine cell. 
         FIG. 37  plots coulombic efficiency versus charging capacity. For a cell with a 0.25 M TBABr pre-soaked electrode and a 2.5 M ZnBr 2  (with 1 wt. % PEG 200 ) electrolyte cycled at 0.5 A/g, Coulombic efficiency decreases substantially when the cell is overcharged, due to a finite quantity of complexing agent. 
         FIG. 38  shows overcharging ZnBr 2  Cells. Overcharging the ZnBr 2  chemistry causes a bromide/tribromide redox shuttle to develop, which creates a temporary internal short circuit to prevent overvoltage and protect the electrodes and electrolyte from degradation. 
         FIGS. 39( a )-39( b )  shows self-balancing of series-connected ZnBr 2  Cells. Two cells, A and B, connected in series are cycled and the stack potential is measured between the counter electrode (CE) and working electrode (WE). The reference electrode (Ref) placed at the Cell A/Cell B junction enables the individual cell potentials to be measured as well. (left) A typical galvanostatic charge/discharge profile is shown for Cell A, Cell B, and the series AB stack for the 100 th  cycle. (right) Cycles 1, 25 and 50 after the cells are intentionally offset (Cell A initially fully discharged and Cell B pre-charged to 50 mAh/g) so that Cell B is overcharging on each subsequent cycle show the profiles re-converge due to self-balancing in the cell stack. 
         FIG. 40  is a schematic of a bipolar stack of ZnBr 2  pouch cells. Exploded view of the components used to construct a bipolar cell stack in a CB-PE composite pouch format. The insulating plastic (polyethylene) and the CB-PE current collectors (carbon black/polyethylene composite) are joined after assembly by heat sealing the cells&#39; edges. Although not diagrammed, the electrodes are pre-soaked in 0.25 M TBABr and separators and electrodes are saturated with electrolyte containing 2.5 M ZnBr 2  and 1 wt. % PEG 200 . External pressure is applied to the entire assembly by binder clips or similar compressive springs. 
         FIG. 41  shows cycling stability of the bipolar stack. When charged to 100 mAh/g, the stack delivers a specific energy of 160 Wh/kg, normalized to the mass of the carbon electrodes, and a Coulombic efficiency of 96.5%. After 1000 cycles, the stack retains 99% of its initial energy. 
         FIG. 42  shows cycling stability of the CTAB/ZnBr 2  cell. A cell with a 0.25 M CTAB pre-soaked electrode and a 2.5 M ZnBr 2  (with 1 wt. % PEG 200 ) electrolyte shows stable cycling at different operating conditions and high Coulombic efficiency. Specific energy is normalized to the dry mass of the activated carbon electrode. 
         FIG. 43  is a flowchart illustrating a method fabricating an energy storage device. 
         FIGS. 44( a )-44( b )  illustrate hybrid EDLC technology according to one or more embodiments of the present invention combines performance advantages of batteries and capacitors. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     In the following description of the preferred embodiment, reference is made to the accompanying drawings that form a part hereof, and in which is shown by way of illustration a specific embodiment in which the invention may be practiced. It is to be understood that other embodiments may be utilized and structural changes may be made without departing from the scope of the present invention. 
     Technical Description 
     The current disclosure provides an energy storage device including an EDLC having at least two electrodes in contact with a redox-enhanced electrolyte that comprises an integral active component for charge storage. For example, the redox-enhanced electrolyte can include two redox couples, such that there is a different one of the redox couples for each of the electrodes (e.g., positive and negative electrodes). By replacing an inert electrolyte with the redox-enhanced electrolyte, additional faradaic charge storage mechanisms can be added to the underlying capacitive ones, as discussed herein. The energy storage device of the present disclosure can increase capacity by utilizing previously “unused” electrolyte mass for energy storage, while maintaining the power and charge-discharge cyclability for appropriate redox-active couples. The energy storage device of the present application also includes aqueous electrolytes and less-expensive carbons, both of which can lower the costs relative to non-aqueous systems. 
     The EDLC of the present disclosure can provide a redox-enhanced electrolyte including two redox-couples that can significantly improve the energy density of the EDLC. In an example, when charged, a first redox-couple of the electrolyte can be adsorbed on a first electrode and a second redox-couple of the electrolyte can be adsorbed on a second electrode, therefore preventing rapid self-discharge. The EDLC of the present disclosure can retain the key advantages of EDLCs while incorporating Faradaic energy-storage without using ion-selective membrane separators. In an example, the EDLC of the present disclosure can exhibit energy densities from 10 to 65 Wh/kg (based on total electrode mass) and stable capacities for greater than 7,000 cycles. Theoretically, this could range from 5-100 Wh/kg. 
     The redox-enhanced electrolyte can be a mixed solution including the two redox couples, which integrate both Faradaic and capacitive energy storage in the same device. The electrodes can become polarized when charged and retard diffusion of the oppositely-charged redox ions to mitigate self-discharge, such that the EDLC does not need an ion-selective membrane as a separator. During charging, the redox-enhanced electrolyte evolves into both a catholyte including a first redox couple and an anolyte including a second redox couple (as shown in  FIGS. 1 and 2 . The EDLC of the present disclosure is fundamentally different form previous devices, including pseudo-capacitors, batteries and Nafion-containing capacitors. 
     Prior to applying a charge to the electrodes, the redox-enhanced electrolyte includes a first redox couple and a second redox couple mixed together. However, once a charge is applied to the electrodes, a portion of the charge is transferred to the first redox couple and the second redox couple. As discussed herein, when the charge is transferred to the first and second redox couples, the solubility of the redox couples change, such that they adsorb on their respective charged electrode surface. In other words, when charged, an anolyte including a first redox couple is formed and adsorbed on the surface of a negative electrode and a catholyte including a second redox couple is formed and adsorbed on the surface of a positive electrode. As used herein, “adsorbed” can be defined as the adhesion of ions or molecules to a surface and pores of carbon electrodes, which creates an insoluble film of the adsorbate on the surface of the adsorbent. Above, the word catholyte is synonymous with “reduced form of the redox couple undergoing redox reactions at the positive electrode—a species that is oxidized during charge and reduced during discharge” and anolyte is synonymous with “oxidized form of the redox couple undergoing redox reactions at the negative electrode—a species that is reduced during charge and oxidized during discharge”. Catholyte and anolyte can also refer to each redox couple, and do not necessarily refer to only one oxidation state of the couple. 
       FIG. 1  illustrates an energy storage device  10  during charging and  FIG. 2  illustrates the energy storage device  10  during discharging, in accordance with at least one example. The energy storage device  10  can include at least two electrodes, for example, a negative electrode  12  and a positive electrode  14  (referred to herein collectively as “electrodes  12 ,  14 ”). 
     In an example, the electrodes  12 ,  14  can include a porous material. For example, the electrodes  12 ,  14  can include one or more of, but are not limited to, activated carbons, carbide derived carbons, carbon nanotubes, mesoporous carbons, graphenes, reduced graphene oxides, metal oxides, and conducting polymers. In one example, the electrodes  12 ,  14  can include activated carbon. In an example, the electrodes  12 ,  14  can have a porosity within a range of about 300 square meter per gram (m 2 /g) to about 3000 m 2 /g. For example, the electrodes  12 ,  14  can have a porosity within a range of about 1500 m 2 /g to about 2500 m 2 /g, such as 1600 m 2 /g, 1700 m 2 /g, 1800 m 2 /g, 1900 m 2 /g, 2000 m 2 /g, 2100 m 2 /g, 2200 m 2 /g, 2300 m 2 /g, and 2400 m 2 /g. Because the redox-enhanced electrolyte contributes substantially to the charge storage capacity of the device and the surface of the carbon participates in the absorption phenomena that prevents self-discharge, carbons for redox-EDLCs can include both reasonably large surface areas but also large pore volumes and thus lower overall densities than those typically used for traditional non-redox EDLC devices. 
     The electrodes  12 ,  14  can include other components such as binders, conductive additives, and porogens. In an example, the binders can be selected from, but not limited to, polytetrafluoroethylene (PTFE), polyvinylidene difluoride (PVDF), and poly-ionic liquids. In an example, the conductive additives can be selected from, but not limited to, acetylene black, graphene, reduced graphene oxide, and carbon nanotubes. 
     As shown in  FIGS. 1 and 2 , the EDLC  10  can include a redox-enhanced electrolyte  16  including a first redox couple  18  and a second redox couple  20 . As discussed herein, the redox-enhanced electrolyte  16  can be a single electrolyte that upon charging can evolve into both an anolyte and a catholyte such that a first redox couple  18  is positioned along a surface of a first electrode  12  and the second redox couple  20  is positioned along a surface of the second electrode  14 . The first redox couple  18  is labeled On/Rn (e.g., anolyte) and can be used at the negative electrode  12 . The first redox couple  18  can be reduced upon charging, and oxidized upon discharge. The second redox couple  20  is labeled Op/Rp (e.g., catholyte) and can be used at the positive electrode  16 . The second redox couple  20  can be oxidized upon charging and reduced upon discharge. 
     As discussed herein, the redox-enhanced electrolyte  16  can be aqueous, organic, or an ionic liquid and include the first redox couple  18  and the second redox couple  20 . The first redox couple  18  for the negative electrode  12  can have standard potentials at or slightly more-cathodic than the hydrogen evolution potential, as well as high solubility and solution compatibility with the catholyte. To minimize or prevent rapid self-discharge, the first redox couple  18  can have a positive charge and physically adsorb on the negative electrode  12  (e.g., activated carbon) following charging. 
     The second redox couple  20  for the positive electrode  14  can have a reduction potential near, or slightly more positive/anodic than, the oxygen evolution potential to maximize energy density, as well as high solubility and solution compatibility with the anolyte. To minimize or prevent rapid self-discharge, the second redox couple  20  can have a negative charge and physically adsorb on the positive electrode  14  (e.g., activated carbon) following charging. 
     In an example, the first redox couple  18  can include a viologen and the second redox couple  20  can include a halide (e.g., bromide). In an example, the first and second redox couples  18 ,  20  do not comprise a metal. The metal-free redox couples are advantageous because they can be less expensive, easier to recycle, do not form dendrites, and are less environmentally harmful. The first redox couple  18  and the second redox couple  20  can be chosen such that the first and second redox couples  18 ,  20  operate at a different potential. 
     Viologens are derivatives of 4,4′-bipyridyl. An example of the dicationic 4,4′-bipyridinium portion of a viologen is shown below. 
     
       
         
         
             
             
         
       
     
     Examples of this viologen are methyl viologen (R=methyl), ethyl viologen (R=ethyl), benzyl viologen (R=benzyl), and pentyl viologen. These viologens have been isolated as salts of the chloride (Cl − ), bromide (Br − ), acetate (CH 3 CO 2   − ) tetrafluorborate (BF 4   − ), perchlorate (ClO 4   − ), triflurormethanesulfonate (CF 3 SO 3   − ), tetraphenylborate (BPh 4   − ), and hexaflurophosphate (PF 6   − ), to name a few. Each of redox couples for methyl, ethyl, heptyl, and benzyl are stable in neutral conditions. The SCE is the standard calomel electrode. 
     In an example, the first redox couple  18  can include one of methyl viologen and heptyl viologen. The standard potentials for methyl and heptyl viologens are at or slightly more-cathodic than the hydrogen evolution potential. In an example, a concentration of the first redox couple  18  can be within a range from about 0.1 molar (M) to about 5 M, such as 0.1 M. 
     In one example, the second redox couple  20  can include bromide (Br − ), which is generally inexpensive and highly soluble (greater than 1 M). Further, aqueous reduction potential of bromide is located above the thermodynamic oxygen evolution potential. In an example, a concentration of the second redox couple  20  can be within a range of about 0.1 M to about 5M, such as about 0.4 M to about 1 M. 
     The EDLC of the present disclosure can retain the key advantages of EDLCs while incorporating Faradaic energy-storage without using ion-selective membrane separators. In an example, the EDLCs of the present disclosure can deliver power densities &gt;3 kW/kg, based on mass of electrodes and electrolyte, which sets them apart from many energy storage technologies. Conventional EDLCs can have a voltage that varies linearly with the state of charge, so the galvanostatic charge-discharge curves are triangular, which can be undesirable for many applications. The ELDCs of the present disclosure exhibit EDLC behavior initially, then transition to battery like behavior at higher voltages, delivering a desirable steady voltage. Together, these properties can provide the high power density of supercapacitors along with the constant potential and high energy density of batteries. 
     1. First Example: Mechanism of Reversible Solid Complex Formation on Both Cathode and Anode 
     Like the viologens, bromide has proven an efficient catholyte in electrochemical energy storage systems, particularly in aqueous flow batteries. However, since the evolution of bromine gas is toxic and corrosive, quaternary ammonium salts are frequently used in bromine flow batteries to complex bromine/Br 3   − , reducing the activity and vapor pressure. 
     Because of the structural similarity between these complexing agents and viologens, the present disclosure describes (1) a viologen anolyte that may also participate in the complex formation with Br 3   −  at the cathode, and (2) each viologen having different length of alkyl substituents will complex with Br 3   −  at varying degree of interaction and adsorption to the electrode. The inventors suspect MV will complex Br 3   −  less efficiently due to its shorter, less hydrophobic, substituent R (=methyl) in aqueous environments. The degree of complexation between HV and MV with chemically generated Br 3   −  was investigated through UV-Vis. ( FIG. 3( a ) ). As expected, UV-Vis results reveal that ca. 15% more of HV complexed/precipitated with Br 3   −  than MV. 
     The inventors postulate that strong adsorption of HV 2+ ·.2Br 3   −  to the cathode as a solid complex enables suppression of the reactivity and diffusion of bromine/Br 3   −  as well as improves electrochemical reversibility of the bromide redox couple. This may explain why the HV/Br cell is stable while the MV cell is not. 
     As described herein, the previously unstable MV/Br system was tested in order to confirm the above described rationale (but with modifications that reflect the rationale). A MV/Br cell with excess bromide (4 times the MV concentration) was constructed and the concentration of MV was increased. In addition, the state of charge was reduced by operating the cell to 1.32 V instead of 1.4 V (as done previously). These operating conditions greatly facilitate the formation, complexation, and adsorption of Br 3   −  to the cathode. Original capacity fade with the MV/Br system was characterized by a 60% loss over 300 cycles. However, much improved stability (10% capacity loss over 2000 cycles) was observed when the cell was operated to 1.32 V with excess concentration of MV and Br −  (see  FIG. 4 ). The results presented herein with the newest MV/Br cell supports the rationale described herein for the operating mechanism of viologen bromide system. 
     As noted previously, the degree of adsorption of charged redox product through complexation should also contribute to the difference in self-discharge between MV and HV systems. Previously, the retarded self-discharge for the halides could not be explained purely by electrostatics, and was attributed to physical adsorption of Br 3   −  within the activated carbon surface, preventing cross diffusion. The present disclosure now suggests that it is actually the HV 2+  dication that holds Br 3   −  better at the cathode through film formation. Together with the film-forming property of HV + . with Br −  at anode, the charged products HV + . and Br 3   −  are all efficiently retained at the surface, inside the pores of the electrodes, and thus provide exceptionally low self-discharge and high coulombic efficiency. 
     Thus, the study presented herein suggests that the successful operating mechanism of the HV/Br system is actually attributable to two electroprecipitation processes occurring simultaneously at both electrodes. Through electroprecipitation, each ion acts as a charge-storing redox couple at one electrode and as a complexing agent at the other electrode (Scheme 1). 
     
       
         
         
             
             
         
       
     
     2. Second Example: Pentyl Viologen as an Anolyte 
     For redox ECs, higher redox active electrolyte concentrations are needed to maximize faradaic energy storage. The free volume in the porous carbon electrodes and the separator determines the volume of electrolyte available. This volume, along with the concentration of the redox-active electrolytes, determines the maximum possible number of ions available for faradaic charging. Consequently, better device performance requires a more concentrated electrolyte to minimize electrolyte mass but still maintain a large reservoir of each redox couple. 
     In order to efficiently replace sparingly soluble HV for the redox EC, the substitute viologen must (1) be easy to synthesize, (2) have high solubility (&gt;1 M) in the oxidized dication state (for energy density), (3) precipitate as a solid film when reduced to the cation radical at anode (for better Coulombic efficiency and self-discharge), and (4) form an insoluble complex with Br 3   −  at cathode (for stability, Coulombic efficiency and self-discharge). These criteria are challenging because long hydrophobic alkyl chains necessary for (3) and (4) work against (2) in an aqueous system. 
     As shorter alkyl groups do not form films upon charging, a series of alkyl substituted viologens with chain lengths R&gt;4 were synthesized. Hexyl viologen (R=6) was excluded from further studies because it does not exhibit good solubility (&lt;0.5 M) in the presence of NaBr. Surprisingly, however, butyl viologen (BV, R=4) and pentyl viologen (PV, R=5) exhibit remarkable solubility (&gt;1.5 M), and form insoluble films when reduced to the radical cation. Thus, BV and PV were further investigated for Br 3   −  complexing ability through UV-Vis experiments. 
     As illustrated in  FIG. 6 , PV complexes with Br 3   −  as efficiently as HV. PV was selected for the anolyte as it (1) exhibits remarkable solubility (&gt;1.5 M), (2) forms an insoluble film when reduced to the radical cation, and (3) has competitive Br 3   −  complexing ability as compared to HV. In addition, the standard reduction potential of PV is 0.1 V more cathodic than that of HV, so it is expected to span a wider voltage range than the previous 1.2 V set for HV/Br system. 
     A cell with 0.85 M PV/3 M NaBr electrolyte was tested by galvanostatic charge/discharge cycling. The cell runs stably at 1.15V for over 1000 cycles, but with a limitation: when operating potential increases to 1.2V, the iR drop increased and the cell started fading. In addition, an unexpected hump around 0.25V during discharge was observed at cathode. This behavior became more distinctive when the cell was operated at 1.25V or higher potentials. 
     These interesting shape changes when SOC increases to 1.2 V and 1.25 V may be caused by the following scenarios. Firstly, a solid complex presents in high quantity and gradually blocks the pores in the carbon, thus increasing the cell resistance. Secondly, increased demand for PV 2+  at the negative electrode causes diffusion of PV 2+ , leading to an insufficient amount of complexing agent for Br 3   −  at the positive electrode. As the concentration of PV 2   +  is decreased the equilibrium will shift, and the relative concentration of the ion pair complex will decrease accordingly. 
     
       
         
         
             
             
         
       
     
     As literature reports that strong adsorption improves reversibility of bromine reduction, slowed kinetics can be expected when complex formation is suppressed. Overpotential with bromide redox reaction and larger iR drop are expected. When the operating potential increases, most of the potential increases are indeed reflected at the positive electrode with larger iR drop, although there is an excess of bromide redox active electrolytes that otherwise could have maintained plateau more at positive. This supports the rationale presented herein. 
     Interestingly, performance degradation is mostly not permanent. When the cell potential was held at 0V for 2 h and resumed charge/discharge cycling, 99% of the original capacity was re-generated. 
     3. Third Example: Additional Complexing Agent 
     a. Overview 
     Based on results from the PV cell, the inventors realized that the viologen/bromide system is not yet fully utilized. Approximately 20% of redox active viologen is being consumed at the cathode for complexation. Consequently, less PV is available for faradaic reactions and capacity is not maximized. In order to supplement any shortage of complexing agent when the state of charge is increased, embodiments of the present invention utilize an additional Br 3   −  complexing agent. There are well known Br 2 /Br 3   −  complexing agents, e.g., methyl ethyl morpholinium bromide (MEM) and methyl ethyl pyrrolidinium bromide (MEP), being used for redox flow batteries. However, as opposed to redox flow battery applications where strong adsorption might be detrimental to movement of redox active electrolyte in the system, specific adsorption of redox couples on the electrode surface is critical for redox-EC operation. Considering how strongly Br 3   −  adsorbs to the electrode surface affects the overall performance of the viologen bromide cell, embodiments of the present invention applied the following selection criteria for an alternative complexing agent in the redox EC described herein. Specifically, the complexing agent (1) should not participate redox reaction at anode, (2) should have stronger complexing power for Br 3   −  than PV, preferably the complex formed should exist in solid form, and (3) its complex should be significantly smaller than PV 2+ .2 Br 3   − . 
     Inspired by the discovery reported in the reversible electrochromism applications using aqueous systems of tetrabutylammonium bromide, embodiments of the present invention incorporated tetraalkylammonium salt as a complexing agent in a supercapacitor. In contrast to the complexing agent used for redox Br −  flow battery, it was discovered that certain tetraalkylammonium bromide possessing carbon numbers more than 10 facilitated complex formation in a solid form. In addition, amphiphilic quarternary ammonium salt complex was shown to adsorb well to hydrophobic carbon electrodes and decrease charge transfer resistance for bromide oxidation in aqueous electrolytes. Thus certain tetraalkylammonium salts were considered an ideal candidate for supercapacitor applications as described herein. 
     Readily available and water soluble tetraalkylammonium bromide salts (R 4 N + Br − , where R=propyl, butyl, and pentyl, respectively) were selected. These quarternary ammonium salts were tested first for competitive adsorption vs PV on the activated carbon (AC) as to avoid using additional complexing agent that comes at the expense of sacrificing surface for PV during electrode preparation process. Based on an adsorption test on AC between PV and a series of tetraalkylammonium salts, UV data reveals that tetrapentylammonium salt adsorbs to the surface of AC more strongly than redox active PV. Thus, tetrapentylammonium was excluded for further testing. 
     The complexing ability of tetrabutylammonium bromide (TBABr) and tetrapropylammonium bromide (TPABr) with Br 3   − , in comparison to PV, was tested. Surprisingly and unexpectedly, tetrabutylammonium bromide (TBABr) was found to have higher complexing ability with Br 3   −  than the TPABr and viologens (that were also tested). Presence of TBABr dropped to almost ca. 60% of the PV complexed with Br 3   − . This screening process led to the identification of TBABr as a promising additional complexing agent for redox EC. In contrast, MEP doesn&#39;t have strong complexing ability over any viologens. 
     b. Further Studies of the Properties of Br 3   −  Complexing Agents 
     In order to further support the efficient use of the Br − /Br 3   −  redox couple for aqueous redox ECs, two differently-structured quaternary ammonium salts were selected and compared as complexing agents for Br 3   −  (complexing agent refers to Br 3   −  complexing agent throughout). Asymmetric cyclic methyl ethyl pyrrolidinium bromide (MEPBr), a commonly used complexing agent for aqueous bromine flow batteries, forms a separate oily-phase with Br 3   −  while the symmetric and more hydrophobic tetrabutylammonium bromide (n-Bu 4 NBr; TBABr) is known to form a solid complex. 34,37  Presented herein are studies of how each complexing agent affects the overall performance of the redox ECs, relative to a control system without either additive. 
     Three asymmetric EC cells were constructed, all utilizing the Br − /Br 3   −  redox couple at the positive electrode, with (1) no complexing agent (1.2 M KBr electrolyte), (2) methyl ethyl pyrrolidinium bromide (MEPBr; 1 M KBr+0.2 M MEPBr), and (3) tetrabutylammonium bromide (TBABr; 1 M KBr+0.2 M TBABr), respectively. The negative counter electrode was purely capacitive and oversized to increase capacity so that the positive electrode could reach the Br oxidation potential with a total applied cell voltage of 1 V. 
     The influence of each complexing agent on the electrochemical behavior of the bromide catholyte in redox ECs was determined by galvanostatic charge/discharge (GCD) cycling tests of each asymmetric cell in a three-electrode configuration ( FIGS. 9( a )-9( c ) ). 
     All cells show electrochemical behavior that transitions from capacitive to faradaic energy storage at the positive electrode (orange curve), indicating oxidation of Br −  to Br 3   − , and only a capacitive (linear potential vs time/charge) response at the negative electrode (purple curve) during charging. Notably, there are differences when TBABr is present as a complexing agent as compared to the KBr and KBr/MEPBr cells. For example, a greater potential of zero charge (PZC) was observed for the KBr/TBABr cell (0.26 V) compared to the KBr (0.09 V) and KBr/MEPBr (0.13 V) cells. The more positive PZC with KBr/TBABr electrolyte allows bromide oxidation to occur earlier in the charging stage and increases the ΔV for the capacitive negative electrode, which translates to greater faradaic charge storage at the positive electrode before the arbitrary cell cutoff potential of 1 V is reached ( FIGS. 9( a )-9( c ) ; orange curves). Considering the amphiphilic nature of the tetrabutylammonium cation (TBA + ), 38,39  the inventors reason that TBABr acts as a surfactant and TBA +  adsorbs at the porous carbon electrodes. To verify this hypothesis, contact-angle measurements were conducted. The contact angle for the carbon electrode with a droplet of aqueous TBABr solution is ˜24° smaller compared to a droplet of aqueous KBr solution (138°;  FIG. 17 ). This surfactant behavior may increase wettability of hydrophobic electrodes, and thus facilitate infiltration of hydrophilic bromide catholyte. 39    
     The present disclosure notes that the onset point of the faradaic plateau at the positive electrode is a function of the complexing agent used. The horizontal grey dashed line drawn at 0.7 V in  FIGS. 9( a )-9( c )  makes apparent the largest negative shift in the Br − /Br 3   −  redox potential for the KBr/TBABr cell. Additional cyclic voltammetry shows a redox potential that is consistent with above GCD potential profile result, as well as a reversible redox reaction in the presence of TBABr ( FIG. 18( a ) ). 
     The observed electrochemical behavior can be explained by the reversible formation of [TBA + .Br 3   − ] solid complex that decreases the Br 3   −  concentration at the interface between the electrolyte and the high-surface-area electrode. Both chemical ( FIG. 10( a ) ) and electrochemical ( FIG. 10( b ) ) methods confirm the generation of a [TBA + .Br 3   − ] solid complex. The image ( FIG. 10( a ) ; right vial) visually shows that after complexation induced by TBA + , Br 3   −  is almost entirely removed from the solution. Notably, the solutions with MEPBr (middle vial) and KBr (left vial) retain a yellow tint, demonstrating that a significant concentration of Br 3   −  remains dissolved due to insufficient complexation by MEP +  (and K + , respectively).  FIG. 10( b )  shows electrochemical generation of a solid complex on the surface of a carbon cloth by passing anodic current in a KBr/TBABr electrolyte. The Raman spectrum taken of this solid exhibits an intense band at 169 cm −1 , which corresponds to symmetric stretching vibration of Br 3   − , 40,41  and its spectrum is identical to the Raman spectrum of commercial [TBA + .Br 3   − ] solid complex ( FIG. 10( c ) ). Further characterization of the electrochemically generated [TBA + .Br 3   − ] solid complex in an aqueous system is well-documented elsewhere. 37    
     Strong adsorption of the charged products within the electrodes has been found to be an effective mechanism to prevent cross-diffusion in a full cell. 26  The present disclosure hypothesizes that the complexation strategy described herein may suppress cross-diffusion even more effectively if the [TBA + .Br 3   − ] solid complex is retained in the pores of the high-surface-area carbon electrodes, instead of being formed and precipitating to the bulk solution upon charging. In order to investigate this hypothesis, controlled potential electrolysis with 1 M KBr/0.2 M TBABr solution was performed with an activated porous carbon pellet as the working electrode (denoted as electrolyzed C pellet) to provide a relevant, yet extreme charged state. As a control, an identical activated carbon pellet (denoted as the control C pellet) was separately prepared and infiltrated with same electrolyte solution through repeated vacuum/N 2  steps. 
     Both carbon surfaces were analyzed by scanning TEM (STEM) with the signal being acquired using a high-angle annular dark-field detector (HAADF-STEM). In this imaging mode, the signal contrast scales linearly with sample thickness, and as the square of average atomic number (Z) of atoms in the sample. 42,43  Therefore, for the sample analysis presented here, the higher average atomic number of the bromine-containing [TBA + .Br 3   − ] solid complexes compared to that for porous carbon ensures that such complexes confined in the pores appear as bright regions in the image (Z-contrast imaging).  FIG. 11( a )  shows a scanning TEM (STEM) image of the electrolyzed C pellet. The material displays clear contrast with nm-scale bright clusters that correspond to concentrations of the element Br, which EDX analysis confirms (Table S2). In contrast, the control C pellet shows no high-contrast spots ( FIG. 11( b ) ), and no Br signal was detected by EDX (Table S2). This control image suggests that Br from KBr/TBABr solution is removed during washing steps, and that the bright regions in  FIG. 11( a )  are mainly due to signals detected from collecting electrons scattered by the insoluble bromide-containing [TBA + .Br 3   − ] complex. These data thus show that the [TBA + .Br 3   − ] solid complex generated in-situ during electrolysis is contained in the pores. This complexation approach combined with porous carbon electrodes being used for EDLCs may lead to enhanced stability and slower self-discharge of the bromide-based redox ECs, without using ion-exchange membranes. The present disclosure notes that if a non-porous electrode is used, precipitation of the [TBA + .Br 3   − ] solid complex occurs, which would cause irreversible capacity loss ( FIG. 19 ). 
     In order to test stability and self-discharge rates, asymmetric cells were constructed in the two-electrode cell configuration with a paper separator. In cycling stability tests, the KBr cell lost ˜20% of its specific energy over 500 cycles. In contrast, the KBr/TBABr and KBr/MEPBr cells show no fading over the course of 500 cycles, and produce ˜80% and ˜40% higher energy density compared to the KBr cell, respectively ( FIG. 12( a ) ). Large differences between the cells are further evident from self-discharge tests. The self-discharge rate determined by the open circuit energy efficiency, η R , of the KBr/TBABr cell was substantially lower than that for KBr and KBr/MEPBr cells, retaining 50% of its energy after 10 h at open circuit, η R (10 h)=50%, compared to η R (10 h) of only 1% and 14% for the KBr and KBr/MEPBr cells, respectively ( FIG. 12( b ) ). Importantly, when the KBr cell was charged to 1.2 V to attain a higher capacity, which is closer to that of the KBr/TBABr cell, an even faster self-discharge rate was observed ( FIG. 12( b ) , solid blue vs dashed blue). This result implies that the self-discharge problem with uncomplexed Br − /Br 3   −  redox couple is worsened at higher states of charge, limiting its application in high-performance redox EC devices. The problems with cycling stability and self-discharge are much aggravated at 40° C. for the KBr and KBr/MEPBr cells relative to the KBr/TBABr cell, suggesting that the increased diffusivity of soluble Br 3   −  at high temperatures accelerates the redox shuttle self-discharge mechanism ( FIGS. 12( c ) and 12( d ) ; results for self-discharge tests from 0° C. to 40° C. are summarized in Table S3). 
     These studies demonstrate that charge retention of bromide catholyte, and the stability and self-discharge performances, depend on whether Br 3   −  is uncomplexed, complexed with MEP +  (liquid state), or complexed with TBA +  (solid state). Our results suggest that [TBA + . Br 3   − ] solid complex generated within the electrode pores suppresses cross-diffusion of oxidized bromide and lowers the self-discharge rate. Meanwhile MEPBr, a common complexing agent for bromine flow batteries, barely shows improvement over a cell without a complexing agent. The molecular structure of MEP + , which lacks hydrophobic substituents, appears to provide insufficient complexation/precipitation with Br 3   − , 37  leaving high concentrations of free Br 3   −  in the electrolyte solution (picture in  FIG. 10( a ) ). 
     The question as to whether the decrease in specific energy observed for KBr and KBr/MEPBr cells is temporary due to reversible shuttling/diffusion effects or irreversible fading from chemical reactions was addressed by disassembling tested cells and assessing changes to the structure/morphology of the filter paper separator and carbon-electrode cell components. The separator from the KBr/TBABr cell appeared identical to the pristine paper separator before cycling, while the separators from the other cells are covered with a black solid (see pictures in  FIG. 20 ). Raman spectra collected of the separator from the KBr/TBABr cell shows no clear peaks, and are identical to the Raman spectrum obtained from a pristine separator ( FIG. 13( a ) ). However, Raman spectra of the separators from the KBr and KBr/MEPBr cells show peaks at approximately 1340 cm −1  and 1610 cm −1  which can be assigned to the D band and G band, respectively, of activated carbon. 44  The same peaks are observed for the non-cycled carbon electrode, indicating that the black solid observed in the separator was shed from the electrode. A control experiment where a pristine separator is soaked in Br 2 /Br 3   −  solution (that mimics the charged state of the cell) demonstrated no color change of the separator in the absence of the carbon electrode. 
     Electron microscopy showed that the electrode exhibited little morphology change when cycled in a KBr/TBABr cell ( FIG. 13( d ) ). In contrast, cracks and partial pulverization of carbon particulates are observed on the electrode surface after cycling in KBr ( FIG. 13( c ) ) and KBr/MEPBr electrolytes ( FIG. 13 e   ), providing evidence of carbon electrode degradation and its subsequent deposition onto the separator (TEM images of the positive electrodes after cycling in  FIGS. 21( a )-21( d ) . Elemental analysis by EDX of the positive electrodes from the KBr and KBr/MEPBr cells after cycling further confirm decreased carbon content (relative to F in the inert PTFE binder) compared to the electrode before cycling (Table S4). 
     Based on the experimental results, the present disclosure proposes that electrochemical intercalation induced by reactive bromine/polybromide causes permanent electrode degradation with time and thus irreversible fading of the KBr and KBr/MEPBr cells. 45,46  When TBA +  is present, the concentration of non-complexed Br 2 /Br 3   −  is significantly reduced, thereby slowing irreversible side reactions and largely preventing electrode degradation upon repeated charge/discharge cycles. This TBA + -induced solid complexation suppresses the permanent capacity loss mechanism. Overall, these results show an efficient way to utilize the bromide catholyte with readily available TBABr, the simple addition of which simultaneously addresses the capacity loss as well as self-discharge problems for static bromide-enhanced redox ECs. 
     c. Design of a High-Performance Viologen/Br Dual-Redox EC with the Addition of Tetrabutylammonium Complexing Agent 
     For maximum faradaic energy storage, redox ECs should utilize redox-active electrolytes at both the positive electrode (catholyte) and negative electrode (anolyte) concurrently (dual-redox enhanced electrochemical capacitors; dual-redox ECs). Illustrative embodiments of the present invention choose viologen (V) as a model anolyte to match the redox activity of the bromide catholyte and test the utility of tetrabutylammonium complexing agent in a full cell. For the V/Br systems, (1) cycling stability largely depends on effective bromine storage in the positive electrode, 36  (2) only viologens with hydrophobic substituents, e.g., pentyl (PV) 36  or heptyl viologen (HV), 26  can function as an efficient Br 3   −  complexing agent, limiting the capacity for faradaic energy storage due to their low solubility (e.g., &lt;0.2 M for HV), and thus (3) it is desirable to enhance energy density by using highly soluble viologens to increase the available concentration of anolyte while finding other means to complex Br 3   −  and maintain cycling stability. 
     The present disclosure envisioned that addition of TBABr to V/Br electrolytes should (1) suppress the fading mechanism at the positive electrode and (2) enable the use of more-soluble, short-alkyl-chain viologens at the negative electrode, in order to (3) maintain cycling stability while producing high energy density in a single device. To verify these hypotheses, readily available ethyl viologen (1,1′-diethyl-4,4′-bipyridinium dibromide; EV) was selected as an anolyte due to its high solubility (&gt;2 M) and the stability of EV 2+ /EV. +  redox couple in aqueous electrolytes. 47  Additionally, EVBr 2  shows good solution compatibility with a bromide catholyte (e.g., NaBr) in an analytical voltammetry cell ( FIGS. 22( a )-22( c ) ). 
     First, a control cell with a readily soluble 1.2 M EVBr 2 /3 M NaBr electrolyte, without additional complexing agent, was assembled and tested. Three-electrode GCD profiles show dual faradaic responses at both positive and negative electrodes, corresponding to Br −  oxidation to Br 3   −  and EV 2+  reduction to EV. + , respectively, upon charging ( FIG. 14( a ) ). This cell produced a specific energy of ˜68 W·h/kg at 1 A/g, but the cell capacity faded and only retained 82% of the initial energy over 1000 cycles ( FIG. 14( b ) ). This poor cycle life confirms that short-alkyl-chain viologens do not effectively retain reactive Br 2 /Br 3   − , which decreases cell stability. To improve the cycle life of EV/Br redox ECs, electrolyte design must utilize a Br 3   −  complexing agent that has stronger Br 3   −  complexing capacity than EV. 
     The degree of (solid) complexation of TBABr with Br 3   − , relative to EV, was tested by determining how much EV precipitates from an aqueous Br 3   −  solution with and without this complexing agent additive. The amount of precipitated EV was indirectly quantified by measuring the concentration of the remaining viologen in solution with ultraviolet-visible spectroscopy (UV-vis). 
       FIG. 15  shows that the addition of Br 3   −  decreased the concentration of EV dissolved in the solution by ca. 83% due to precipitation of the nominally [EV 2+ .2Br 3   − ] solid complex (EV′; blue open-square curve vs EV 2+ /Br 3   − ; blue open-circle curve), which still leaves substantial free, non-complexed Br 3   −  present in the solution, causing the poor cycling life of the EV/Br cell. Importantly, when TBABr was added together with Br 3   −  and EV, EV remained completely dissolved (EV 2+ ; blue open-square curve vs EV 2+ /Br 3   − /TBA + ; orange solid curve). These UV-vis results suggest that TBABr has a greater Br 3   −  complexing capacity than EV 2+  and that [TBA + .Br 3   − ] solid complex is preferentially formed. Notably, MEPBr, a common Br 2 /Br 3   −  complexing agent for aqueous flow battery systems, does not induce any solid complexation/precipitation with Br 3   −  in the presence of EV 2+  (EV 2+ /Br 3   − ; blue open-circle curve vs EV 2+ /Br 3   − /MEP + ; black solid curve), which correlates with the poor stability and fast self-discharge results obtained for the previous asymmetric KBr/MEPBr cell. This relative interaction strength, i.e., MEP + &lt;EV 2+ &lt;TBA + , is consistent with previous findings that indicate hydrophobicity enhances solid complexation, 36,37  and suggests that TBABr should be a suitable complexing agent for EV/Br dual-redox ECs. 
     A two-electrode cell with a 1.2 M EVBr 2 /2.88 M NaBr/0.12 M TBABr electrolyte (i.e., 10 mol % addition of TBABr based on the molar concentration of EVBr 2 ), paper separator, and symmetric activated carbon electrodes (areal mass loading of 12.7 mg/cm 2 ) was assembled and tested by GCD. The concentration of EV and Br were set at 1.2 M and 3 M, respectively, for the comparison with standard EV/Br cell, and 10 mol % addition of TBABr ensures that this electrolyte concentration is readily soluble, thus providing simple solution preparation and lower viscosity. The cell (denoted as EV/TBA/Br) produced ˜64 W·h/kg at 1 A/g with ˜97% Coulombic efficiency and a high energy efficiency of ˜84% when charged/discharged between 0 V and 1.35 V. Most importantly, the specific energy of the cell degraded by only ˜3% over 1000 cycles compared to 18% capacity loss of the cell without TBABr cycled under the same conditions ( FIG. 16( a ) ). For the long-term cycling test, the EV/TBA/Br cell maintained stability with 90% energy retention over 5000 cycles (charge/discharge at 2 A/g) and exhibited ˜4% degradation over an additional 7000 cycles when operated from 0 V to 1.3 V at the same current density ( FIG. 16( b ) ). This stability increase shows that the superior performance of short-alkyl-chain viologens can be maintained without sacrificing lifetime through the addition of TBABr. Furthermore, the EV/TBA/Br cell shows good self-discharge characteristics with η R  (6 h)=53% when charged to 1.3 V and η R  (6 h)=45% when charged to 1.35 V. For these two conditions the open circuit voltage losses are only 13% and 16%, respectively, comparable to other redox ECs with costly ion-selective membrane separators ( FIG. 16( c ) ; Table 1). The Ragone plot in  FIG. 16( d )  shows that the EV/TBA/Br cell provides a power performance higher than 3 kW/kg while still retaining ˜15 W·h/kg energy density. This cell&#39;s energy, power, stability, and self-discharge performance are compared with previous reports of aqueous redox ECs in Table 1. To provide further performance comparison, an aqueous EDLC (1 M Na 2 SO 4  electrolyte) and a commercial non-aqueous EDLC (BCAP0001 P270 T01, Maxwell Technologies) were tested as control/comparison devices.  FIG. 16( d )  shows that the EV/TBA/Br cell produced specific energy well above the 1 M Na 2 SO 4  cell (black curve) at all power rates. Compared to the commercial non-aqueous cell, this cell delivered as high as ˜250% increased specific energy over a wide range of power rates up to ˜3 kW/kg. Overall, these results further demonstrate that the EV/TBA/Br redox EC system substantially improves energy as well as power densities of aqueous EDLCs by adding dual faradaic reactions at both the positive and negative electrodes, without negatively impacting cycle life. 
     
       
         
           
               
             
               
                 TABLE 1 
               
             
            
               
                   
               
               
                 Comparison of the (selected) previous reports of aqueous redox ECs 
               
            
           
           
               
               
               
               
               
               
               
            
               
                   
                 Redox 
                 Specific energy 
                   
                   
                 Self-discharge 
                   
               
               
                 Electrode 
                 electrolyte 
                 at W/kg (or A/g) 
                 Cycling stability 
                 Separator 
                 rate 
                 Ref. 
               
               
                   
               
               
                 AC 
                 SnSO 4 / 
                 75 Wh/kg 
                 85% 
                 Anion exchange 
                 1.4 V→1.16 V 
                 19 
               
               
                   
                 VOSO 4   
                 (at 0.055 A/g) 
                 (4500 cycles) 
                 membrane 
                 (10 h) 
               
               
                 AC 
                 EVBr2/ 
                 64 Wh/kg 
                 90% (5000 
                 Filter paper 
                 1.35 V→1.13 V 
                 this 
               
               
                   
                 TBABr/ 
                 (at 1 A/g) 
                 cycles to 1.35 V) 
                   
                 (6 h) 
                 work 
               
               
                   
                 NaBr 
                   
                 96% (7000 
               
               
                   
                   
                   
                 cycles to 1.3 V) 
               
               
                 AC 
                 SnF 2 / 
                 46 Wh/kg 
                 80% 
                 Anion exchange 
                 1.4 V→1.2 V 
                 23 
               
               
                   
                 VOSO 4 / 
                 (at 1 A/g) 
                 (6500 cycles) 
                 membrane 
                 (10 h) 
               
               
                   
                 H 2 SO 4   
               
               
                 Reduced GO 
                 KI/ 
                 44 Wh/kg 
                 ~80% 
                 polypropylene 
                 Not available 
                 31 
               
               
                   
                 KOH 
                 (at 0.83 A/g) 
                 (5000 cycles) 
                   
                 (N/A) 
               
               
                 Functionalized 
                 KBr/ 
                 28.3 Wh/kg 
                 86.3% 
                 Cation exchange 
                 N/A 
                 28 
               
               
                 CNT 
                 Na 2 SO 4   
                 (at 372 W/kg) 
                 (10000 cycles) 
                 membrane 
               
               
                 AC 
                 K 3 Fe(CN) 6   
                 28.3 Wh/kg 
                 80% 
                 Cation exchange 
                 0.8 V → 0.65 V 
                 21 
               
               
                   
                   
                 (at 0.05 A/g) 
                 (9000 cycles) 
                 membrane 
                 (10 h) 
               
               
                 AC 
                 EVBr 2 / 
                 23 Wh/kg 
                 No degradation 
                 polypropylene 
                 N/A 
                 47 
               
               
                   
                 H 2 SO 4   
                 (at 0.25 A/g) 
                 (1000 cycles) 
               
               
                 graphene 
                 hydroquinone/ 
                 8.9 Wh/kg a   
                 80% 
                 Nafion ® 117 
                 0.8 V → 0.3 V 
                 24 
               
               
                 hydrogel 
                 H 2 SO 4   
                 (at 252 W/kg a ) 
                 (1,000 cycles) 
                 membrane 
                 (~1.5 h) 
               
               
                   
                 CuSO 4 / 
                 6.7 Wh/kg a   
                 ~99% 
                 porous cellulose 
                 49% a  of initial 
               
               
                   
                 H 2 SO 4   
                 (at 360 W/kg a ) 
                 (1,000 cycles) 
                 acetate 
                 energy (1 h) 
               
               
                   
               
               
                 Note: 
               
               
                 The data are arranged by descending specific energy reported without considering rates. (GO: graphene oxide; CNT: carbon nanotube) 
               
               
                   a The values are not explicitly reported in the paper, and estimated numbers are from the previously reported literature. 26   
               
            
           
         
       
     
     d. Pentyl Viologen, TBABr, and NaBr System 
     Testing of a comprising an electrolyte consisting of 1M PVBr 2 , 0.1M TBABr, and 3M NaBr, wherein TBABr was used as an additive, produced a specific energy of 43 Wh/kg while maintaining stability, retaining &gt;95% of energy density over 4000 cycles. In addition, still great suppression of self-discharge was obtained despite having a large concentration of complexes at the electrode surface (83% energy retention after 6 h open circuit). 
     To demonstrate the symmetric nature of the device and the mobility of the redox couples, the inventors reversed the polarity of the cell and ran the same cycling tests. The performance is notably unchanged even though the device is being operated “backwards.” 
       FIG. 23( a )  plots galvanostatic cycling of PV/TBABr/NaBr cell with Whatman separator; charged/discharged at a rate of 1 A/g. 
     The performance of the n-alkyl viologen redox-ECs was optimized. The mechanism responsible for the stability of heptyl viologen bromide Gen II chemistry was formalized by the inventors′. This “dual redox couple counterion-induced reversible complexation” mechanism is summarized in  FIG. 23( b ) . Surprisingly and unexpectedly, with an optimized pentyl viologen bromide electrolyte (1 M PV/3 M NaBr), the slow self-discharge and excellent cycling stability of heptyl viologen electrolyte and the high specific energy of the methyl viologen electrolyte could be simultaneously realized in a single system.  FIGS. 23( e )-( f )  illustrate the performance of the optimized pentyl viologen chemistry. 
     In summary, the present disclosure reports on a novel paradigm shift for the conventional use of a mobile, liquid state to complex Br 3   −  and a fundamentally different and unexpected solution for complexing/storing Br 3   −  in aqueous redox ECs. The present disclosure demonstrates with microscopic-level evidence that reversible solid complexation of Br − /Br 3   −  redox couple induced by tetrabutylammonium bromide effectively stores reactive and diffusive bromine within the pores of the carbon electrodes. This mechanism suppresses unwanted chemical reactivity and cross-diffusion of Br 2 /Br 3   −  that results in improved cycling stability and self-discharge rates of redox ECs. As illustrated herein, this fundamental understanding of chemical and electrochemical processes at the electrolyte/electrode interface is used to develop a high-performance dual-redox EC. 
     Specifically, this fundamental understanding of the electrolyte chemistry has led to an improved system highlighting the use of newly synthesized pentyl viologen (PVBr 2 ) with the addition of tetrabutylammonium bromide (TBABr) as an additive complexing agent. Pentyl viologen combines the stability of heptyl viologen with the solubility of methyl viologen while TBABr provides additional Br 3   −  complexing power at cathode. Current system produces record high of 43 Wh/kg with good stability and self-discharge rate 
     This dual-redox EC, which integrates TBABr with an ethyl or pentyl viologen anolyte and a bromide catholyte, produces a record specific energy with stable cycling at high power levels: Addition of tetrabutylammonium surprisingly and unexpectedly improves all aspects of device performance including stability, energy and power density without adding complexity to the fabrication process. The system can be assembled without a dry room or glove box, uses aqueous electrolyte with readily available salts, and has a cost-effective paper separator that avoids the use of expensive ion-selective membranes. These attributes address hurdles to practical commercialization, and low costs of production may be possible. The systematic approach presented herein to efficiently utilize bromide catholyte and design of a high-performance dual-redox EC should be informative and promise to be readily applicable for a wide variety of energy storage applications, especially for the science of hybrid electrochemical capacitors (e.g., bromide catholyte at positive electrode with faradaic battery-type or pseudocapacitive negative electrode). 
     4. Fourth Example: Bipolar Pouch Cell 
     Only carbon-based current collector materials have sufficient corrosion resistance for many aqueous electrolytes, including viologen bromide systems, but the conductivity of these materials is too low for a conventional spirally wound cell.  FIG. 24  illustrates a new bipolar cell design to address this problem. In this design, multiple cells  2400  comprised of activated carbon (AC) electrodes, an electrolyte, a separator  2402 , carbon polymer (C-polymer) composite current collectors  2406  are stacked in a series configuration and current only travels a short distance through the carbon-polymer (C-polymer) composite current collectors  2406  between cells, minimizing the total resistance. The voltage of the series stack (nV cell ) is equal to the voltage V cell  of a single cell multiplied by the number n of cells in the stack. The current collectors between individual cells are bipolar, because one current collector is serving as a positive current collector of one cell and a negative current collector of the adjacent cell. The current collectors on the top and bottom of the stack are not bipolar. Also shown are metal backing  2408  and positive (+) and negative (−) tabs or contacts  2410   a ,  2410   b.    
     Carbon has the additional advantage of better contact resistance with electrode materials due to the lack of a metal oxide passivation layer. It also suppresses hydrogen and oxygen evolution due to large kinetic overpotentials, which in some systems will effectively widen the practical electrochemical stability window of aqueous electrolytes. The use of carbon as a current collector is well-explored. Expanded graphite foil has been shown to be a suitable current collector for aqueous supercapacitors, but one drawback is its porous structure, which makes it permeable to electrolyte. Carbon paper has also been used, but is too fragile for practical use. To get around these problems in flow batteries and fuel cells, electrolyte-impermeable and mechanically strong thermoplastic/carbon composite current collectors are used. However, these materials are thick, rigid plates with flow channels incorporated, making them unattractive for use in compact, portable cells. In non-flow systems, thin, flexible, lightweight carbon/plastic composites would be preferable. The present disclosure has identified a commercially available candidate current collector material known as Caplinq Linqstat XVCF. This is a 70 micrometer thick flexible film of carbon black-impregnated polyethylene (CB-PE) manufactured for antistatic packaging applications with a sheet resistance of 75-500Ω/□. The material costs &lt;$1.6/m 2 , has high mechanical strength and is heat-sealable. These attributes mean that a single low-cost material can serve simultaneously as a mechanical support, bipolar current collector, and seal. 
     The first step in realizing this design was assembling a single-cell pouch using the CB-PE film. The resulting pouch device  2500  is shown in  FIGS. 25 (a 0 - 25 ( d ), and comprises current collectors  2502  (comprising CB-PE film), a separator  2504 , a plastic spacer  2506 , an electrolyte  2508 , and electrodes  2510  and  2511  on either side of the separator. The walls  2512 ,  2514  of the pouch  2500  include the current collectors  2502  and are sealed to the insulating plastic spacer  2506  with a heat-seal  2518 , so that the electrodes  2510  and  2511 , the electrolyte  2508 , and the separator  2504  are sealed within the pouch  2500 . 
     The device shows very similar performance to the same chemistry in a glassy carbon Swagelok cell, as illustrated in  FIG. 26 , and high stability, as illustrated in  FIG. 27 . 
       FIG. 28( a )  illustrates constructing a series stack of 2 of the individual cells from  FIGS. 25( a )-25( d )  so that the middle current collector  2801  is bipolar.  FIG. 28( b )  shows a larger version of cell in  FIG. 28( a )  where the electrodes  2510 ,  2511  are squares measuring 4 cm by 4 cm instead of small 1 cm OD circles.  FIG. 28( c )  shows a cross-sectional view of the inside of the bipolar pouch cell from  FIG. 28( b ) , further illustrating the conducting polyethylene (PE)  2801  and the insulating polyethylene  2506 . Individual bipolar pouch cell stacks could comprise any number of series-connected cells, and are not limited to just two cells, as shown in simplified form in  FIG. 24 . Finally,  FIG. 28( d )  illustrates how multiple (in this case 2) bipolar pouch cell stacks  2500  can be stacked (resulting in this case in a total of four cells in series). Pressurizing the stack between two external metal plates  2804  (e.g., titanium plates) using springs or binder clips  2806  makes a device that can charge to 4.8 V (1.2 V per cell×4 cells). Also shown are positive (+) and negative (−) tabs or contacts. 
     Typical galvanostatic cycling data and a charge/discharge potential profile are shown in  FIGS. 29( a )-29( b ) . 
       FIGS. 30( a )-30( f )  show example cross sections of different pouch cell geometries, wherein one or more of the pouch cell geometries comprise positive current collector a, positive electrode b, separator c, negative electrode d, insulating plastic spacer layer e, heat seal f, negative current collector g, bipolar current collector h, and in the case of  FIGS. 30( e ) and 30( f ) , microporous polyethylene separator i. The cells inside the pouches could be circular, square, or any desired geometric shape. 
     a. Pouch Embodiment 1: Pouch Cell for Viologen Bromide Type System 
       FIG. 30( a )  (single cell) and  FIG. 30( b )  (multiple cell stack) show typical cross sections of pouch cells for a viologen bromide system which have both a positive and a negative electrode. Here the separator is larger than the electrodes but smaller than the aperture of the insulating plastic spacer. This geometry could work with any battery or supercapacitor that has solid positive and negative electrodes and solid active materials, a redox-active electrolyte, or a combination of the two. 
     b. Pouch Embodiment 2: Pouch Cell for a Zinc Bromine Type System 
       FIG. 30( c )  (single cell) and  FIG. 30( d )  (multiple cell stack) show typical cross sections of a pouch cells for zinc bromine systems, which have only a positive electrode (the negative electrode is eventually deposited as zinc metal from the electrolyte inside the separator). Here the separator is larger than the positive electrode and larger than the aperture of the insulating plastic spacer, but still smaller than the heat-sealed perimeter of the cell. This partial overlap of the separator by the spacer helps prevent zinc metal dendrites from growing around the edge of the separator. Such an overlap could be used in the example illustrated in  FIG. 30( a )  as well, but is less necessary in the case of viologens or other battery or supercapacitor systems. 
     The pouch embodiment illustrated in  FIG. 30( a )  comprises thick insulating plastic spacers while the pouch embodiment illustrated in  FIG. 30( b )  comprises thin plastic spacers, but the thick and thin spacers could be interchanged between the two designs. Thin spacers cause the current collectors to deform more to meet for the heat seal, therefore thicker spacers may be preferable for stacks of large numbers of cells. Thick spacers keep the current collectors flatter and more parallel so that the outermost current collectors do not have to bend as dramatically. 
     Multiple cell stacks could mean 2 cells in series to 10&#39;s of cells in series. As discussed herein (see e.g.,  FIG. 28( d ) ), multiple pouches each comprising multiple stacked cells can also be connected together in parallel or series configurations in a larger final battery pack. 
     c. Pouch Embodiment 3 
       FIG. 30( e )  shows how the separator c and insulating plastic spacer e could be integrated into one component by using a microporous polyethylene separator i. The micropores M of the polyethylene collapse in the region of the heat-seal, making that region impermeable to electrolyte and serving the same function typically addressed by the plastic spacer. This design provides a simplified construction, better separation of the two sides of the cell, and better mechanical properties. It may also enable the use of binder-less electrode slurries that fill the entirety of the two separated sealed compartments, instead of typical freestanding electrode films/pellets that must be solid to avoid flowing around the edge of the separator and shorting the cell. 
     d. Pouch Embodiment 4 
       FIG. 30( f )  shows the microporous polyethylene separator concept adapted for a zinc bromine system, where instead of a negative electrode d there is a second separator c with large porosity to provide volume for the zinc metal to deposit into. 
     Only single cells are shown in pouch embodiments 3 and 4; however, pouch embodiments 3 and 4 may also be adapted to multi-cell stacks as in pouch embodiments 1 and 2. 
     The outer surfaces of the positive and negative current collectors can be covered in a conductive grease and contacted with metal foils or metal plates acting as terminals to an external circuit. External pressure can optionally be applied to the entire stack to improve electrical contact at all of the interfaces. 
     
       
         
           
               
             
               
                 TABLE 2 
               
             
            
               
                   
               
               
                 Comparison of bipolar pouch and commercial supercapacitor 
               
            
           
           
               
               
               
            
               
                   
                 Bipolar Pouch Prototype 
                 Commercial Supercapacitor 
               
               
                   
                   
               
            
           
           
               
               
               
            
               
                 Electrolyte 
                 Aqueous (2.5 V) 
                 Organic (2.7 V) 
               
               
                 Dimensions 
                 H: 2.5 mm; W/L: 40 mm 
                 H: 40 mm; OD: 18 mm 
               
            
           
           
               
               
               
               
               
            
               
                 Mass 
                 6 
                 g 
                 13 
                 g 
               
               
                 Volume 
                 4 
                 cm 3   
                 10 
                 cm 3   
               
               
                 Energy 
                 48 
                 mWh 
                 51 
                 mWh 
               
               
                 Specific Energy 
                 8 Wh/kg 
                 (12 Wh/L) 
                 3.9 Wh/kg 
                 (5.1 Wh/L) 
               
               
                 Specific Power 
                 1 kW/kg 
                 (1.5 kW/L) 
                 3 kW/kg 
                 (4 kW/L) 
               
            
           
           
               
               
               
            
               
                 Temperature 
                 −5° C. to 55° C. 
                 −40° C. to 65° C. 
               
               
                   
               
            
           
         
       
     
     5. Fifth Example: Aqueous Bromide Redox-ECs with a Zinc Metal Anode 
     The TBABr complexing agent paired with activated carbon and the bromide/tribromide redox couple makes a very stable and energy-dense aqueous cathode that functions well with all viologens investigated thus far. To see if this cathode could be more broadly useful, the cathode was paired with a zinc metal anode instead of an activated carbon/viologen anode. Zinc is an ideal anode because it operates in the same mildly acidic pH range, is low cost, has an extremely cathodic standard reduction potential (−0.76 V vs. SHE), and possesses a very high overpotential for hydrogen gas evolution. Although zinc bromine flow batteries often use quaternary ammonium complexing agents to sequester Bra, the strong complexing agents like TBABr will not work with a traditional zinc bromine battery because the tetrabromozincate ion, [ZnBr 4 ] 2− , will form and precipitate as an insoluble complex with TBA +  out of solution. To solve this issue, the inventors pre-adsorbed the TBABr complexing agent to the activated carbon by soaking the positive electrode in a solution of ˜0.25 M TBABr ( FIG. 31 ). The soaked electrode is then put into contact with a paper separator saturated with ≥5 M ZnBr 2 . As the ZnBr 2  diffuses into the electrode, the (TBA) 2 [ZnBr 4 ] solid complex forms and precipitates out of solution, adsorbing as thin film on the activated carbon surface. The full cell assembly consists of a 280 μm-thick Norit A Supra activated carbon positive electrode and a 180 μm-thick Whatman #1 paper separator between two current collectors. The typical final electrolyte is ˜2.5 M ZnBr 2  with 1 wt. % PEG 200  (200 MW polyethylene glycol) additive to suppress zinc dendrite growth. In some cells an additional 0.5 M concentration of NaBr is added as a supporting electrolyte. 
     While charging, bromide is oxidized to tribromide at the positive electrode, which complexes with TBA +  and forms a solid at the electrode surface. This can also be seen as the tribromide anion replacing the tetrabromozincate anion in the solid complex. There is no need for an activated carbon negative electrode because zinc is plated directly from the electrolyte as a solid metal deposit on the negative current collector, filling the porous separator with zinc metal. Both of these processes are reversed upon discharge of the cell ( FIG. 32 ). The solid complexation of tribromide by TBA +  dramatically slows self-discharge compared to a ZnBr 2  cell without TBABr due to suppression of cross-diffusion ( FIG. 33 ). 
     The zinc bromine cells constructed according to the methods described herein are typically charged by galvanostatic cycling at 1 A/g to a capacity of 100 or 150 mAh/g, based on the mass of the carbon electrode. They are discharged to a cell voltage of 1 V. The zinc bromide chemistry, compared to the viologen systems, is less redox-EC and more battery. A typical galvanostatic cycling with potential limitation (GCPL) profile, shown in  FIG. 34 , has exceptionally flat charge/discharge plateaus, a low iR drop, and coulombic efficiencies of 96-98%. The high 1.8 V potential of this chemistry is excellent for aqueous electrolytes and ˜50% higher than that of the viologen systems. Due to the large capacity and high operating potential, the system exhibits excellent specific power and specific energy. To measure energy-power performance, a series of discharge rate tests was performed at discharge currents ranging from 1 A/g dry  to 20 A/g dry  ( FIG. 35 ). The zinc bromine cells have only one electrode, so a discharge current of 20 A/g dry , for example, is plotted as 10 A/g dry  for comparison with viologen cells that contain two electrodes, since the areal current density is equivalent. The same data were also normalized to the mass of the wet cell stack including electrode, electrolyte, and separator and compared to that of viologen cells in  FIG. 36 . Although the ZnBr 2  devices cannot be charged as quickly as viologen redox-ECs, the maximum discharge energy and discharge power are significantly higher (40 Wh/kg wet  and 4 kW/kg wet , respectively). 
     The ZnBr 2  cells have finite complexing agent, so when they are overcharged and all of the TBA +  is utilized in TBABr 3  solid complexation, additional Br 3   −  can escape the positive electrode uncomplexed and diffuse across the cell where it is reduced back to Br, causing Coulombic efficiency to decrease as charging capacity increases ( FIG. 37 ). Fortunately, this process is non-destructive. In fact, the development of this redox-shuttle is useful for when multiple cells are connected in series. If one cell in a series stack becomes overcharged, it will enter a condition where the Br − /Br 3   −  redox shuttle develops and forms a temporary internal short circuit until the other cells in the stack reach the same fully charged state ( FIG. 38 ). 
     Therefore, the chemistry has a built-in mechanism for self-balancing that does not require water splitting (gassing) that would typically be used for a lead-acid battery, or a battery management system (BMS) that would typically be used for lithium-ion packs. To show experimentally that series-connected cells can stay balanced, two individual cells were connected and cycled together at 1 A/g to 100 mAh/g, as shown in  FIGS. 39( a )-39( b ) . The cells stayed balanced over 100 cycles, with each cell completing the faradaic plateau at the end of every discharge. The cycling test was then repeated with the cells intentionally offset (Cell A initially fully discharged and Cell B pre-charged to 50 mAh/g) so that Cell B was overcharged on each subsequent cycle. Over the course of 50 cycles, the cells re-balanced, the potential profiles returned to their initial equilibrium state, and cycling continued normally. 
     A bipolar pouch comprised of two cells was next constructed using zinc bromine chemistry to investigate cycling stability in a system more complex than individual cells. The exploded view of the cell components before heat-sealing and compression is shown in  FIG. 40 .  FIG. 40  illustrates the device comprises rigid plate  4000 , metal foil or plate  4002 , conductive grease  4004 , positive and negative current collectors  2502 , insulating plastic  2506 , electrodes  2510 ,  2511 , separators  2504 , and bipolar current collector  2801 . The positive (+) and negative (−) terminals are also shown. After assembly, the stack was cycled at 1 A/g to a capacity of 100 mAh/g. The system showed excellent stability, with approximately 99% capacity retention over 1000 cycles ( FIG. 41 ). 
     To demonstrate that this concept can function with other bromine complexing agents, another CB-PE pouch cell was built with cetyltrimethylammonium bromide (CTAB) instead of TBABr. The cell was charged to 150 mAh/g at different rates and only 3% capacity fade was observed over more than 3000 cycles ( FIG. 42 ). 
     6. Process Steps 
       FIG. 43  is a flowchart illustrating a method of fabricating an energy storage device such as an electrochemical capacitor, supercapacitor, or EDLC, or a supercapacitor/battery hybrid. 
     Block  4300  represents providing or fabricating a first electrode  12  and a second electrode  14  (e.g., an anode and a cathode). In one or more examples, the cathode comprises carbon. In one or more further examples, the cathode comprises carbon and the anode comprises carbon. 
     In one or more embodiments, the step comprises providing a pouch  2500  having a first wall  2512  and a second wall  2514 , the first wall and the second wall each including a current collector comprising a carbon-polymer composite  2502 . The electrodes  2510 ,  2511 , electrolyte  2508  and separator  2504  are disposed inside the pouch  2500 . 
     Block  4302  represents providing an electrolyte  16  between and in contact with the electrodes  12 ,  14 . 
     In one or more embodiments, the electrolyte comprises an integral active component for storing a charge. 
     In one embodiment, the electrolyte includes a first redox couple  18  comprising a halogen or halide (e.g., bromine, bromide, iodine, iodide, bromine moiety, iodine moiety) and a second redox couple  20  comprising a viologen. In one or more examples, the halogen is provided in a compound, e.g., NaBr or KBr in cases where the halogen is bromine. 
     In yet a further embodiment, the first redox couple comprises bromine (or bromine moiety) and the electrolyte comprises a complexing agent, such as a viologen or a tetraalkylammonium, tetraalkylammonium compound or moiety (e.g., but not limited to, tetrabutylammonium bromide in cases where the halogen in the first redox couple is bromine, or tetrabutylammonium triiodide or tetrabutylammonium tribromide in the cases where the halide is iodide) that forms a complex with the halogen (e.g., bromine, bromine moiety, iodine, iodine moeity) in the catholyte. In one example, the tetrabutylammonium bromide combines with the bromine or bromine moeity in the catholyte so as to form a [TBA + .Br 3   − ] solid complex retained in the pores of the porous carbon material in the cathode. In another embodiment wherein the complexing agent comprises a viologen, the viologen forms a complex with the bromine or bromine moiety in the catholyte. In one example, the electrolyte comprises 10 mol % of TBABr to the molar concentration of EVBr 2 . 
     Examples of the viologens used herein include a viologen having the structure: 
     
       
         
         
             
             
         
       
     
     wherein R is an alkyl. 
     In one or more examples wherein the anolyte and/or the catholyte comprise viologen or viologen moiety, the viologen is at least one compound selected from ethyl viologen, butyl viologen, pentyl viologen, hexyl viologen, and other viologens comprising an alkyl having at least four carbon atoms. 
     In yet a further embodiment, the electrolyte includes a zinc moiety such as zinc halide (e.g., ZnBr 2 ) and tetraalkylammonium complexing agent (including, but not limited to tetrabutylammonium bromide (TBABr) or cetyltrimethylammonium bromide (CTAB)) is pre-adsorbed/pre-soaked on the cathode. In one example with the electrolyte comprising zinc halide, the electrolyte does not comprise a viologen. 
     In one or more zinc bromine system embodiments, the TBABr or CTAB pre-adsorption solution has a TBABr or CTAB concentration in a range of 10 mM to 1 M, the electrolyte comprises a ZnBr 2  concentration in a range of 1 M to 9 M and comprises an amount of PEG200 additive in a range of 1000 ppm to 100,000 ppm (0.1 wt. % to 10 wt. %), although other additives may also be used. In one or more further zinc bromine embodiments the electrolyte may further comprises an NaBr supporting electrolyte wherein the NaBr concentration is in a range of 0 M to 3 M. Other salts could also work (KBr, etc.). The supporting electrolyte may provides extra conductivity and additional bromide source. 
     Block  4304  represents providing additional EDLC or supercapacitor/battery hybrid components, if necessary. In one pouch embodiment, the step comprises sealing (e.g., heat sealing, in which case the carbon-polymer composite may comprise a thermoplastic) a plastic spacer  2506 , the electrodes  2510  and  2511 , the electrolyte  2508 ,  16 , and a separator  2504  inside the pouch  2500 . The seals  2518  are formed between the wall  2512  and the plastic spacer  2506 , and the second wall  2514  and the opposite side of the plastic spacer  2506 . The compartment bound above and below by the walls  2512  and  2514  and on the edges by the inside of the plastic spacer  2506  houses the two electrodes  2510  and  2511 , the separator  2504 , and the electrolyte  2508  permeating the electrodes and separator. Multiple such pouches can be stacked to get the desired stack voltage. In this embodiment, walls/current collectors  2512  and  2514  from adjacent cells can be in direct contact, as shown in  FIG. 28 d   , or can be replaced by a single bipolar wall/current collector  2801  as shown in  FIGS. 28 a    and  28   c.    
     In one or more embodiments, the first wall  2512  and the second wall  2514  are flexible and have a thickness of 100 micrometers or less. 
     In one or more embodiments wherein the pouch is sealed using heat-sealing, the heat sealing comprises melting the walls  2512 ,  2514  and spacer  2506  together with no adhesive and with no additional sealing. 
     In one or more embodiments, the separator and the spacer are made from one component with a microporous polymer separator that has porosity collapse in the region of the heat-seal (see e.g.,  FIGS. 30( e ) and 30( f ) ). 
     Block  4306  represents the end result, an energy storage device including, but not limited to, an EDLC, an EC, a battery, or supercapacitor/battery hybrid. 
     In one or more embodiments, during charging, the electrolyte evolves into a catholyte including the first redox couple and an anolyte including the second redox couple. When charged, the charge is stored in Faradaic reactions with the first and second redox couples in the electrolyte and in a double-layer capacitance of a porous carbon material that comprises at least one of the electrodes. In one or more embodiments, synergistic electrodes tune the pore size and volume of the carbon in the electrodes. 
     In an embodiment wherein the electrolyte comprises zinc halide:
         during charging, the zinc or zinc moiety from the zinc halide plates onto the anode and the halogen in the halide oxidizes so as to form a solid complex (e.g., (TBABr 3   − ]) with the tetraalkylammonium on the cathode; and   when charged, the charge is stored in Faradaic reactions with the electrolyte and in a double-layer capacitance of a porous carbon material in the cathode.       

     7. Advantages and Improvements 
     As described herein, viologen and bromide were identified as promising dual redox-active electrolytes for aqueous redox ECs. Bromide is a promising high-performance redox-active species for aqueous redox-enhanced electrochemical capacitors (redox ECs) due to the reversible redox reaction of Br − /Br 3   − , excellent solubility and high redox potential. 
     With methyl viologen (MV) and bromide as the electrolytes, the system delivered a specific energy of ˜50 Wh/kg dry , but performance faded with prolonged cycling. Substituting heptyl viologen (HV) for MV dramatically improved cycling stability and slowed the self-discharge rate without the use of an ion-selective membrane separator. Improved performance of HV/Br over MV/Br was attributed to the strong adsorption of the charged HV + . onto the activated carbon electrode. However, the specific energy of HV/Br system was ˜20% lower than MV/Br system due to the low solubility of HV (&lt;0.2 M). The critical challenge was to increase the solubility of a redox active viologen and still maintain stable cycling and slow self-discharge through strong adsorption. Since the development of promising HV/Br system, the present disclosure has investigated the viologen/bromide system in detail to understand the underlying mechanism, and to further improve the system. 
     The advantages of bromine as a catholyte are offset by the corrosive and volatile Br 2 /Br 3   −  generated and its crossover through a separator. Asymmetric quaternary ammonium salts are conventionally used in flow batteries to complex Br 2 /Br 3   −  as a mobile, oily-liquid phase and reduce the reactivity and vapor pressure. As demonstrated herein, this practice is not effective for static redox ECs. Instead, the present disclosure proposes stable bromine charge storage using tetrabutylammonium bromide as a complexing agent. In contrast to liquid complexation, this cation induces the reversible phase transition of soluble Br 3   −  into an insoluble solid complex and physically confines it in the pores of carbon electrodes upon charging. This mechanism suppresses unwanted chemical reactivity and cross-diffusion, leading to better stability and slower self-discharge for bromide-based aqueous redox ECs—without the use of an expensive ion-selective membrane separator. Based on this new mechanistic insight on the utilization of solid-state bromine storage in redox ECs, the present disclosure developed a dual-redox EC consisting of a bromide catholyte and a viologen anolyte with the addition of tetrabutylammonium bromide. For example, in comparison to aqueous and organic electric double-layer capacitors, the system using ethyl viologen and tetrabutylammonium bromide enhances energy by a factor of ca. 11 and 3.5, respectively, with a specific energy of ˜64 W·h/kg at 1 A/g, a maximum power density &gt;3 kW/kg, and cycling stability over 7000 cycles. 
     Furthermore, example systems disclosed herein are simple to fabricate in ambient conditions, use aqueous electrolyte, which is in principle safer, and provide further potential for higher power density due to the lower ionic resistance. 
     Conventional supercapacitors deliver high power for short periods of time, while conventional batteries deliver low power for long periods of time. Designing to these extremes requires tradeoffs on safety, lifetime, and cost. Embodiments of the EDLCs presented herein, on the other hand, integrate battery level energy density with capacitor level durability and power density into one safe, low cost device. Applications include using embodiments of the EDLCs described herein in an electrical grid or microgrid (e.g., with renewables), transportation (electric buses, engine start-stop, regenerative braking), and for industrial applications (energy recovery, heavy equipment, and fork lifts). Examples of the EDLC technology presented herein are well positioned to compete with advanced lead acid batteries by delivering higher power and longer life time at lower cost (see  FIGS. 32( a ) and 32( b ) ). 
     
       
         
           
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                 Comparison of redox EDLC embodiments and other technologies 
               
            
           
           
               
               
               
               
               
               
            
               
                   
                 Redox EDLC 
                 Redox EDLC 
                   
                   
                   
               
               
                   
                 (Demonstrated) 
                 (Proposed) 
                 Lithium-Titanate 
                 Ultracapacitor 
                 Lead Acid 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
               
            
               
                 Cycle 
                 &gt;20,000 
                 100,000 
                 6,000 
                 1,000,000 
                 1,000 
               
               
                 lifetime 
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
            
               
                 Charging 
                 2 
                 min 
                 1 
                 min 
                 10 
                 min 
                 10 
                 sec 
                 8 
                 h 
               
               
                 time 
               
               
                 Specific 
                 1.5 
                 kW/kg 
                 4 
                 kW/kg 
                 3 
                 kW/kg 
                 10 
                 kW/kg 
                 0.2 
                 kW/kg 
               
               
                 power 
               
               
                 Specific 
                 12 
                 Wh/kg 
                 17.5 
                 Wh/kg 
                 30-80 
                 Wh/kg 
                 6 
                 Wh/kg 
                 18 
                 Wh/kg 
               
               
                 energy 
               
            
           
           
               
               
               
               
               
               
               
            
               
                 Cost 
                   
                   
                 &lt;$500/kWh 
                 $1500/kWh 
                 $2000/kWh 
                 $200/kWh 
               
               
                   
               
            
           
         
       
     
     8. Supplementary Information 
     a. Methods and Materials Used for the Third Example (TBABr Complexing Agent with Ethyl Viologen Bromide Dual Redox Active Electrolyte) 
     Chemicals— 
     All reagents and starting materials were obtained commercially and used as received without any further purification: 
     Sodium bromide (NaBr), sodium sulfate (Na 2 SO 4 ), tetrabutylammonium bromide (TBABr), 1-ethyl-1-methylpyrrolidinium bromide (methyl ethyl pyrrolidinium bromide; MEPBr), and ethyl viologen dibromide (EVBr 2 ) were purchased from Sigma-Aldrich. Hydrobromic acid (HBr) was purchased from Acros Organics, tetrabutylammonium tribromide was purchased from Alfa Aesar, sodium bromate (NaBrO 3 ) was purchased from J. T. Baker Chemical Co., sodium hydroxide (NaOH) was purchased from Fisher Chemical, and potassium bromide (KBr) was purchased from EMD Chemicals Inc. Water was from a Milli-Q Simplicity™ 185 system with resistivity ≥18.2 MΩ·cm (if not specified, all solutions in the SI and text refer to aqueous solutions). 
     Carbon Electrodes— 
     Activated carbon was prepared by CO 2  activation of high-purity carbon fibers (Donacarbo S-241, Osaka Gas Co., ˜13 μm OD×130 μm long) in a tube furnace at 890° C. under flowing CO 2  (100 SCCM) for 22.5 h. Detailed characterization data, including specific surface area, elemental composition and pore size distribution were reported previously. 1    
     For the preparation of electrodes, activated carbon, polytetrafluoroethylene (PTFE) binder (60 weight % aqueous dispersion from Sigma-Aldrich), and acetylene black conductive additive (Vulcan® XC72R) were mechanically mixed with a 90:5:5 mass ratio with isopropanol, and the resulting slurry was rolled into a single freestanding film with a PTFE rolling pin. This film was dried overnight at 160° C. in air, ground into a powder through a mesh sieve, and further dried under high vacuum at room temperature for two days. Freestanding electrode pellets were pressed from the powder in a 1-cm-diameter die (MTI Corporation) on a Carver hydraulic press under an applied uniaxial force of 2 tons, applied 3 times. Electrodes were 1 cm in diameter and 300±5 μm thick, for a total volume of 0.024 cm 3 , and density of 0.42 g/cm 3 . 
     Electrolytes— 
     The electrolytes were prepared by dissolving EVBr 2  and/or bromide salts in 18.2 MΩ water. 
     Tribromide (Br 3   − ) Solution— 
     Bromine and Br 3   −  were generated using the following chemical reactions: 2  
 
NaBrO 3 +5Br − +6H + →3Br 2(aq) +3H 2 O
 
Br 2(aq) +Br − ⇄Br 3   − (K eq =16.1M −1 )
 
     Cell Design and Assembly— 
     The construction of the redox-enhanced electrochemical capacitor (redox EC) cell including cell housing, current collectors, and the cell stack with two electrodes and a separator is described in detail in a previous report by the inventors. 3  Briefly, a two-electrode cell was built from a perfluoroalkoxy (PFA) Swagelok fitting with glassy-carbon-capped current collectors. For the preparation of each cell stack, two electrodes were soaked in 1.5 mL of test electrolyte, and vacuum and N 2  (150 psi) were alternately applied to infiltrate the hydrophobic carbon electrodes with aqueous electrolyte. Electrodes were then placed on either side of an electrolyte-wetted, 12-mm-diameter filter paper separator (Whatman™ #1). Thereafter, the cell stack was pressed between the two glassy-carbon-capped current collectors inside the cell body. For the three-electrode configuration tests, a T-shaped Swagelok PFA union was used with an Ag/AgCl reference electrode (Fisher Scientific™ Accumet™) placed with the tip at the edge of the separator with ˜0.5 mL of excess test electrolyte added to submerge the reference electrode frit. 
     b. Electrochemical Studies 
     All electrochemical experiments (cyclic voltammetry, controlled potential electrolysis, and galvanostatic charge/discharge cycling test) were performed on a Bio-logic VMP3 potentiostat/galvanostat. 
     Analytical Voltammetry— 
     The cyclic voltammetry experiments were carried out in a conventional three electrode cell with either glassy carbon (CH Instruments, 3 mm diameter) or activated carbon pellet (identical to carbon electrode used in cells; pasted on a carbon cloth with conducting grease) working electrode, a Pt wire counter electrode, and an Ag/AgCl reference electrode (CH Instruments). The glassy carbon electrode was polished using polishing alumina (0.05 μm), and the Pt wire electrode was rinsed first with acetone followed by water and methanol, and then dried before each experiment. Test solutions were purged with N 2  for 10 mins prior to each measurement. 
     Controlled Potential Electrolysis— 
     Electrolysis experiments were performed in an open beaker-type cell with 6 mL of test electrolyte, i.e., 1 M KBr/0.2 M TBABr solution. Either carbon cloth, graphite rod or an activated carbon pellet (identical to carbon electrode used in cells; pasted on a carbon cloth with conducting grease) served as working electrodes and a platinum wire served as the counter electrode. An Ag/AgCl electrode was used as the reference electrode. 
     Electrochemical Characterization of Redox ECs— 
     All galvanostatic charge/discharge (GCD) cycling tests were performed at a temperature of 25±1° C., or in a temperature chamber for temperature-dependent studies. The applied current for GCD cycling tests was normalized to the combined dry mass (activated carbon, carbon black, and PTFE binder) of both positive and negative electrodes. Potential limits were applied with the voltage range from 0 V (for discharging) to various V max  values (for charging). Energy and power reported in the text indicate discharge energy (E dis ) and average discharge power (P dis ), which are normalized to the dry mass of both positive and negative electrodes to get specific energy (W·h/kg) and specific power (W/kg), respectively. The following equations are used for calculating device performance (I=applied current, t=time, and V=voltage): 
     
       
         
           
               
               
               
             
               
                   
                   
               
             
            
               
                   
                 Charge capacity, Q ch  (mA · h) 
                 Q ch  = I ch  · t ch   
               
               
                   
                 Discharge capacity, Q dis  (mA · h) 
                 Q dis  = I dis  · t dis   
               
               
                   
                 Coulombic efficiency, η C   
                 η C  = Q dis /Q ch   
               
               
                   
                 Charge energy, E ch  (W · h) 
                 E ch  = ∫ 0   t     ch    I ch  · V(t) dt 
               
               
                   
                 Discharge energy, E dis  (W · h) 
                 E dis  = ∫ 0   t     dis    I dis  · V(t) dt 
               
               
                   
                 Average discharge power, P dis  (W) 
                 P dis  = E dis /t dis   
               
               
                   
                   
               
            
           
         
       
     
     The self-discharge rate was quantified based on the remaining discharge energy as a function of open circuit time, δ. An open circuit energy efficiency, η R , is defined as the ratio of the energy retained after time δ at open circuit to the initial discharge energy and calculated by the following formula: 
     
       
         
           
               
               
               
             
               
                   
                   
               
             
            
               
                   
                 Open circuit energy efficiency, η R   
                 η R (δ) = E dis (δ)/E dis (0) 
               
               
                   
                   
               
            
           
         
       
     
     Other Characterization Methods 
     The UV-vis spectra were acquired on an Agilent 8453 UV-vis spectrophotometer equipped with a cuvette holder. All spectra were recorded under ambient conditions with a 1 cm light-path. Contact angle measurements were taken on a DataPhysics OCA 15Pro system using an automatic elliptical fitting program, and the images were recorded with a charge-coupled device (CCD) camera horizontal to the drop to allow measurements of the test electrolytes&#39; contact angles on the sample surface. Raman spectroscopy was performed on a Horiba JY Aramis Raman microscope equipped with a CCD detector thermoelectrically cooled to −70° C. Raman spectra were recorded with the incident laser of 0.86 mW, 600-μm hole, 400-μm slit width and a 600 lines/mm grating. The structure/morphology changes of carbon materials were observed through electron microscopes of a FEI Titan operating at 300 kV in scanning TEM mode, a FEI Quanta 600 SEM, and a FEI TECNAI™ T20 high-resolution transmission electron microscope (TEM) operating at 200 kV. The elemental composition of positive electrodes and carbon pellets was analyzed by energy-dispersive X-ray spectroscopy (EDX) at an accelerating voltage of 24.4 kV. 
     c. Normalized Performance Metrics 
     When the performance of devices including redox ECs is reported, normalizing to the dry mass of both positive and negative electrodes is the common practice in the literature. Therefore, the inventors evaluated cell performance normalized by dry mass in the present disclosure so that direct comparisons can be made. However, the inventors note that the redox couples in the electrolyte significantly contribute to the capacity through faradaic energy storage for the redox ECs. To clarify and address this discrepancy of the performance normalization, the inventors have included a table (Table S1) which normalizes energy, power, and capacity to both masses, i.e., performance metrics based on “wet” cell mass (electrodes plus electrolyte) and “dry” cell mass (electrodes only). 
     Performance Normalization— 
     Electrodes and electrolyte from a 1.2 M EVBr 2 /0.12 M TBABr/2.88 M NaBr two-electrode cell massed before and after cycling weighed 90 mg. The cell performance was then normalized to the total masses of electrodes only (indicated as g), and electrodes plus electrolyte (indicated as g wet ) in Table S1. 
     
       
         
           
               
             
               
                 TABLE S1 
               
             
            
               
                   
               
               
                 Performance metrics normalized to different cell components 
               
               
                 (cell was charged/discharged between 0 V and 1.35 V 
               
               
                 at 1 A/g. Energy, capacity, and power reported here are from 
               
               
                 the 20 th  charge/discharge cycle.) 
               
            
           
           
               
               
               
            
               
                   
                 Dry electrodes 
                 Wet electrodes 
               
               
                   
                   
               
            
           
           
               
               
               
            
               
                 Mass for 
                 20 mg (Cathode: 10 mg; 
                 90 mg (Electrolyte: 70 mg; 
               
               
                 normalization 
                 Anode: 10 mg) 
                 electrodes: 20 mg) 
               
               
                 (mg) 
               
            
           
           
               
               
               
               
               
            
               
                 Specific energy 
                 63.6 
                 W · h/kg 
                 14.1 
                 W · h/kg wet   
               
               
                 (W · h/kg) 
               
               
                 Specific capacity 
                 66.6 
                 mA · h/g 
                 14.8 
                 mA · h/g wet   
               
               
                 (mA · h/g) 
               
               
                 Specific power 
                 970 
                 W/kg 
                 216 
                 W/kg wet   
               
               
                 (W/kg) 
               
               
                   
               
            
           
         
       
     
     d. Further Experimental Details 
     Contact-Angle Measurements (Figure S1)— 
     Aqueous solutions of 1 M KBr, 1 M MEPBr, and 1 M TBABr were prepared, and an activated carbon pellet (identical to carbon electrode used in cells) was used as a test surface. A 2 μL liquid droplet of test electrolyte was gently placed on the surface with a syringe, and the needle was withdrawn immediately to minimize any inconsistency that might be caused by solution evaporation prior to image capture. The contact angle was determined by using an automatic elliptical fitting program. 
     Controlled Potential Electrolysis, Scanning Transmission Electron Microscopy (STEM), and Energy-Dispersive X-Ray Spectroscopy (EDX) (Table S2)— 
     To demonstrate the electrochemical generation of the [TBA + .Br 3   − ] solid complex, anodic oxidation of bromide was carried out with a carbon cloth as working electrode. To an open beaker-type cell was added 6 mL of 1 M KBr/0.2 M TBABr solution, and controlled potential electrolysis at 1.2 V (vs Ag/AgCl reference electrode; a Pt wire counter electrode) was performed until yellow solids were clearly visible on the working electrode. Following electrolysis, the working electrode was photographed and its image is displayed in  FIG. 10   b.    
     To investigate solid-state confinement of electrochemically generated [TBA + .Br 3   − ] solid complex in the pores of the high-surface-area carbon electrode, analysis of carbon surface/pores was conducted using STEM following electrolysis. For the electrolysis, a high-surface-area activated carbon pellet was pasted and pressed on a carbon cloth with conducting grease. The remaining area of the carbon cloth was masked with electrochemical tape to block its exposure to the electrolyte. As a control, an identical activated carbon pellet was separately prepared. Both pellets were immersed in the 1 M KBr/0.2 M TBABr solution, and vacuum/N 2  (150 psi) were alternately applied to infiltrate the hydrophobic carbons with aqueous electrolyte. Then, electrolysis was performed with the first pellet (electrolyzed C pellet) as the working electrode in an open beaker-type cell with 1 M KBr/0.2 M TBABr solution at set potential of 0.6 V (vs Ag/AgCl reference electrode; a Pt wire counter electrode). The potential increased incrementally to 1.2 V before the electrolysis was terminated after a charge of 10.4 C was passed. For the full duration of electrolysis, the control pellet (control C pellet) was immersed in a separate 1 M KBr/0.2 M TBABr solution. 
     Both carbon pellets were removed from the solutions and each surface was washed with water, soaked in 10 mL of water for 7 h, and dried in air at room temperature for 24 h. Samples for STEM analysis were prepared by sonicating (10 mins) small pieces of each pellet in isopropanol and drop-casting the dispersion onto lacey-carbon TEM grids. The samples were imaged by STEM with the signal being acquired using a high angle annular dark field detector (HAADF-STEM). In addition, elemental analysis by EDX of the electrolyzed C pellet and control C pellet were performed and results are summarized in Table S2. 
     
       
         
           
               
             
               
                 TABLE S2 
               
             
            
               
                   
               
               
                 Elemental analysis by EDX of the electrolyzed C pellet 
               
               
                 and control C pellet (relative atomic ratio of C to Br 
               
               
                 present in the sample; calculation based on the atom %) 
               
            
           
           
               
               
               
               
            
               
                   
                 Sample 
                 C 
                 Br 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                   
                 Electrolyzed C pellet 
                 28 
                 72 
               
               
                   
                 Control C pellet 
                 100 
                 0 
               
               
                   
                   
               
            
           
         
       
     
     UV-Vis Measurements for Testing Complexation of Ethyl Viologen Dication (EV 2+ ) and Br 3   −  ( FIG. 15 )— 
     To generate spectra of uncomplexed EV 2+ , 20 mM EVBr 2  solution was prepared in a 1.5 mL centrifuge tube, and the solution was agitated with a vortex mixer for 1 min followed by centrifugation for 5 min at 4,000 rpm (Eppendorf® MiniSpin Plus Centrifuge). Then, a 5 μL sample of the 20 mM EVBr 2  solution was diluted 400 times into 1.995 mL of water in a quartz cuvette. The capped cuvette was shaken to ensure a homogeneous analyte before UV-vis measurements. 
     To generate spectra of the EV 2+  after complexation with Br 3   − , 500 μL of 60 mM EVBr 2  solution was combined with equal volumes of 120 mM Br 3   −  solution and water. Then, EV remaining dissolved in the supernatant after the addition of Br 3   −  was processed with the same methods stated above before UV-vis measurements. Optical absorption data for both uncomplexed and complexed EV 2+  samples were normalized to the absorbance at the absorption maxima (λ max =260 nm) for the uncomplexed EV 2+  sample. 
     UV-Vis Measurements for Testing Complexation of EV 2+  and Br 3   −  in the Presence of Methyl Ethyl Pyrrolidinium Bromide (MEPBr) and Tetrabutylammonium Bromide (TBABr) ( FIG. 15 )— 
     To generate spectra of the EV 2+  in the presence of Br 3   −  and MEPBr or TBABr, respectively, to test competitive Br 3   −  complexation between EV 2+  and these quaternary ammonium cations, 500 μL of 60 mM EVBr 2  solution was combined with equal volumes of 120 mM Br 3   −  solution and 120 mM quaternary ammonium bromide solution in a 1.5 mL centrifuge tube. Then, EV remaining dissolved in the supernatant was processed with the same methods stated above before UV-vis measurements. Each spectrum was normalized by the absorption maxima measured for uncomplexed EV 2+  samples (in a solution containing the corresponding concentrations of MEPBr and TBABr, respectively, but without Br 3   − ). 
     Control/Comparison Devices ( FIG. 16 d   )— 
     An aqueous EDLC cell (1 M Na 2 SO 4  electrolyte) and commercial non-aqueous device (BCAP0001 P270 T01, Maxwell Technologies) were tested to provide reference performance data in comparison to the EV/TBA/Br dual-redox EC. The 1 M Na 2 SO 4  cell was assembled with the same cell housing, current collectors, electrodes, and separator as the EV/TBA/Br cell. The commercial cell was tested with a specified 2.7 V of working potential range. To report specific energy and specific power of the Maxwell cell normalized to the dry mass of both positive and negative electrodes, the device was disassembled after GCD cycling tests. The extracted cell stack was placed in 20 mL aqueous NaOH solution to dissolve the aluminum foil current collectors and isolate the electrodes. Thereafter, the electrodes were soaked in ˜20 mL of doubly distilled water and dried in an oven at 160° C. until the mass remained constant. 
     e. Supplementary Data 
     
       
         
           
               
             
               
                 TABLE S3 
               
             
            
               
                   
               
               
                 Open circuit energy efficiency (η R ) for each asymmetric cell at 0° C., 25° C., and 40° C. 
               
               
                 (Self-discharge rates) 
               
            
           
           
               
               
               
               
            
               
                   
                   
                 1M KBr/0.2M 
                 1M KBr/0.2M 
               
               
                 Open circuit energy 
                 1.2M KBr cell 
                 MEPBr cell 
                 TBABr cell 
               
            
           
           
               
               
               
               
               
               
               
               
               
               
            
               
                 efficiency, η R  (□ h) 
                 0° C. 
                 25° C. 
                 40° C. 
                 0° C. 
                 25° C. 
                 40° C. 
                 0° C. 
                 25° C. 
                 40° C. 
               
               
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
               
            
               
                 η R  (2 h) (%) 
                 43 
                 40 
                 8 
                 63 
                 66 
                 44 
                 80 
                 79 
                 70 
               
               
                 η R  (6 h) (%) 
                 20 
                 5 
                 0 
                 44 
                 34 
                 9 
                 67 
                 62 
                 49 
               
               
                 η R  (10 h) (%) 
                 10 
                 1 
                 0 
                 32 
                 14 
                 2 
                 59 
                 50 
                 37 
               
               
                   
               
            
           
         
       
     
     
       
         
           
               
             
               
                 TABLE S4 
               
             
            
               
                   
               
               
                 Elemental analysis by EDX of positive electrodes after cycling (relative 
               
               
                 atomic ratio of C to F; calculation based on the atom %) 
               
            
           
           
               
               
               
               
            
               
                   
                 Cells 
                 C 
                 F 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                   
                 Pristine activated carbon electrode 
                 97 
                 3 
               
               
                   
                 Electrode after cycling in a KBr cell 
                 83 
                 17 
               
               
                   
                 Electrode after cycling in a KBr/MEPBr cell 
                 84 
                 16 
               
               
                   
                 Electrode after cycling in a KBr/TBABr cell 
                 98 
                 2 
               
               
                   
                   
               
            
           
         
       
     
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     CONCLUSION 
     This concludes the description of the preferred embodiment of the present invention. The foregoing description of one or more embodiments of the invention has been presented for the purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise form disclosed. Many modifications and variations are possible in light of the above teaching. It is intended that the scope of the invention be limited not by this detailed description, but rather by the claims appended hereto.