Systematic Study of Quaternary Ammonium Cations for Bromine Sequestering Application in High Energy Density Electrolytes for Hydrogen Bromine Redox Flow Batteries

Bromine complexing agents (BCAs) are used to reduce the vapor pressure of bromine in the aqueous electrolytes of bromine flow batteries. BCAs bind hazardous, volatile bromine by forming a second, heavy liquid fused salt. The properties of BCAs in a strongly acidic bromine electrolyte are largely unexplored. A total of 38 different quaternary ammonium halides are investigated ex situ regarding their properties and applicability in bromine electrolytes as BCAs. The focus is on the development of safe and performant HBr/Br2/H2O electrolytes with a theoretical capacity of 180 Ah L−1 for hydrogen bromine redox flow batteries (H2/Br2-RFB). Stable liquid fused salts, moderate bromine complexation, large conductivities and large redox potentials in the aqueous phase of the electrolytes are investigated in order to determine the most applicable BCA for this kind of electrolyte. A detailed study on the properties of BCA cations in these parameters is provided for the first time, as well as for electrolyte mixtures at different states of charge of the electrolyte. 1-ethylpyridin-1-ium bromide [C2Py]Br is selected from 38 BCAs based on its properties as a BCA that should be focused on for application in electrolytes for H2/Br2-RFB in the future.


Introduction
Within the last ten years, numerous chemical combinations of negative and positive half-cell chemistries for redox flow battery application have been published. The majority of these compositions have been investigated on laboratory scale [1-3]. One commercialized and noticeable redox flow battery system for stationary energy storage application is the hydrogen bromine redox flow battery (H 2 /Br 2 -RFB) [4][5][6].
One of the challenges attributed to the H 2 /Br 2 -RFB application is the high vapor pressure of bromine in the electrolyte solutions commonly used in this system [7]. In this study, 38 cost-effective additives based on quaternary ammonium halide salts are investigated for their applicability as bromine complexing additives (BCA) and their effects on electrolyte properties. The most promising additive is selected for further investigation in a cell. This systematic investigation is carried out for the first time for electrolytes in H 2 /Br 2 -RFBs.

State of the Art
In this flow battery system, the negative half cell resembles the negative half cell of a proton exchange membrane fuel cell anode, but is operated in a reversible mode. Liquid posolytes based on hydrobromic acid (HBr), bromine (Br 2 ) and water (H 2 O) are pumped through the positive half cell, while bromide (Br − ) is oxidized to Br 2 during charge operation (Equation (1)) and vice versa during discharge operation [4,5,8]. In some research articles, gaseous positive half cells operating with bromine vapor are also discussed [4]. The thermodynamic cell voltage is 1.09 V [9]. Br 2 itself is hardly soluble in water [10][11][12][13][14]. Nevertheless, if bromide ions are present, Br 2 forms polybromides such as tribromide (Br 3 − ), pentabromide (Br 5 − ) or higher polybromides Br 2n+1 − [13,15,16] following Equation (2): Br − (aq) + n Br 2 (aq) Br 2n+1 − (aq) (2) Bromine and bromide form addition bondings by complexation, resulting in the previously mentioned polybromide cations Br 2n+1 − [17]. Complexation allows the maintaining of high concentrations of Br 2 in aqueous bromide solutions. These electrolytes are particularly interesting for the application of Br 2 /Br − electrolytes in RFBs due to their high theoretical energy density of up to 254 Wh L −1 and a theoretical volumetric capacity of up to 233 Ah L −1 (HBr 48 wt%). Ideally, in order to achieve high power densities in H 2 /Br 2 -RFBs, high concentrations of HBr and Br 2 are indispensable [18]. Nevertheless, Br 2 itself and in polybromide form is already quite volatile at ambient temperature [19][20][21] and can react with different electrode and cell components of the H 2 /Br 2 -RFBs [4,[22][23][24][25][26]. One major concern is the crossover of Br 2 from the positive to the negative half cell during cell operation. When Br 2 comes into contact with the platinum-based catalysts in the hydrogen half cell, it can induce corrosive dissolution of platinum resulting in the formation of bromoplatinates [4,[22][23][24][25][26]. The decay of the H 2 electrode catalyst can be avoided by reducing the concentration of Br 2 in the positive half cell electrolyte.
Stabilization of polybromides by conversion into a less volatile form would reduce the bromine vapor pressure, thus leading to a safer battery electrolyte [7]. Additives used to lower bromine's volatility have been applied in zinc bromine RFB (Zn/Br 2 -RFB) [8,[27][28][29][30][31][32][33][34][35][36][37][38][39] and vanadium bromine RFB (V/Br 2 -RFB) [40,41] electrolytes for a long time. These additives are mostly based on organic quaternary ammonium cation compounds and are called bromine complexing agents (BCA). Their bromide or chloride salts are usually highly soluble in aqueous electrolytes. However, their polybromide salts are only slightly soluble or even insoluble in aqueous media [33,36,42]. A further advantage of the polybromide salts of quaternary ammonium BCAs is their low melting point, leading to an insoluble ionic liquid at room temperature. In the electrolytes, these liquids form emulsions that coalesce over time by forming a heavy second phase in the electrolyte [36], as shown in Equation (3). For illustration, Figure 1 shows a photo of an electrolyte solution with a two-phase liquid Br − /Br 2 /H 2 O/ [BCA] + electrolyte in the center.

Work Plan
In this work, we investigate 38 quaternary ammonium halides ex situ as prospective BCAs for their suitability for application in Br − /Br2 electrolytes. The aim is to obtain electrolytes for the positive half cell of a H2/Br2-RFB with a theoretical volumetric capacity of 180 Ah L −1 . All investigated BCAs are shown in Table 1. They comprise of substances from six building blocks: (i) pyridines, (ii) pyrrolidines, (iii) morpholines, (iv) piperidines, (v) 3-methylimidazoles and (vi) tetraalkylammonium compounds. In this research article, the abbreviations listed in Table 1 are used for simplicity. In this study, the BCAs are examined for solubility in the electrolyte, the stability of a second liquid phase at room temperature and their bromine binding strength for a defined electrolyte composition. BCAs that do not form a stable liquid second phase are either not soluble in the electrolyte or show too low bromine binding strength and are excluded from a detailed study as they are not suitable for a battery application. BCAs, which are still of interest, are intensively investigated over the entire state of charge (SoC) range of the electrolyte with a focus on battery performance-relevant parameters: stability, concentration of Br2 in the aqueous electrolyte, redox potential as well as the electrolytic conductivity of the aqueous phase. For the Comprehensive work on BCAs has been carried out for Zn/Br 2 -RFB electrolyte mixtures and the properties have been described by Cathro et al. [42], Eustace [36] and Lancry et al. [31]. While the work on BCAs for Zn/Br 2 -RFB electrolytes is extensive and only a few studies applying BCAs in V/Br 2 -RFB have been published so far, no systematic study is available on the application of BCAs in HBr/Br 2 /H 2 O electrolytes for H 2 /Br 2 -RFB. In addition, the influence of the different polybromides on the electrolyte properties has not been investigated and is hardly documented in the literature for Zn/Br 2 -RFB [17].

Work Plan
In this work, we investigate 38 quaternary ammonium halides ex situ as prospective BCAs for their suitability for application in Br − /Br 2 electrolytes. The aim is to obtain electrolytes for the positive half cell of a H 2 /Br 2 -RFB with a theoretical volumetric capacity of 180 Ah L −1 . All investigated BCAs are shown in Table 1. They comprise of substances from six building blocks: (i) pyridines, (ii) pyrrolidines, (iii) morpholines, (iv) piperidines, (v) 3-methylimidazoles and (vi) tetraalkylammonium compounds. In this research article, the abbreviations listed in Table 1 are used for simplicity. In this study, the BCAs are examined for solubility in the electrolyte, the stability of a second liquid phase at room temperature and their bromine binding strength for a defined electrolyte composition. BCAs that do not form a stable liquid second phase are either not soluble in the electrolyte or show too low bromine binding strength and are excluded from a detailed study as they are not suitable for a battery application. BCAs, which are still of interest, are intensively investigated over the entire state of charge (SoC) range of the electrolyte with a focus on battery performance-relevant parameters: stability, concentration of Br 2 in the aqueous electrolyte, redox potential as well as the electrolytic conductivity of the aqueous phase. For the first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br 2 on the polybromides tribromide (Br 3 − ), pentabromide (Br 5 − ) and heptabromide (Br 7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H 2 /Br 2 -RFB. The principle of this selection process is depicted in Figure 1. Table 1. Quaternary ammonium halides for investigation of their properties as bromine complexing agents represented by their structure, name and abbreviation (bold). Letters in brackets identify substances that are synthesized at Fraunhofer ICT (S) and are used from commercial suppliers (C). Details are mentioned in the Supplementary Materials (SM).

Quaternary Ammonium Compounds Used as BCAs
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1. Table 1. Quaternary ammonium halides for investigation of their properties as bromine complexing agents represented by their structure, name and abbreviation (bold). Letters in brackets identify substances that are synthesized at Fraunhofer ICT (S) and are used from commercial suppliers (C). Details  1,1,1-Trimethyl-1-n-hexadecylammoniumbromide, [CTA]Br (C) first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.   first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1. first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1. first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1. first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  (C) first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1. first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
first time, detailed investigations regarding parameter development are carried out on the basis of the measured distribution of Br2 on the polybromides tribromide (Br3 − ), pentabromide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
[C23MPy]Br (S) mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
mide (Br5 − ) and heptabromide (Br7 − ) in the aqueous phase. Properties of the fused salt phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Quaternary Ammonium Compounds used as BCAs
phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  phase are not discussed in detail here in order to retain the clarity of the article. However, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.  fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

1-Ethyl-3-methylimidazol-1iumchloride, [C2MIm]Cl (S)
1-n-Propyl -3-methylimidazol-1iumbromide, fused salt generally has low conductivity [36] and is therefore not the preferred option for cell applications. The criteria are defined to select a BCA for the application; the observed phenomena are explained in detail, and lastly, one BCA is selected for further use in a H2/Br2-RFB. The principle of this selection process is depicted in Figure 1.

Stabiltiy of Two-Phase Electrolytes and Bromine Binding Strength of BCAs
A total of 38 BCAs are synthesized for this work (marked with "(S)" in Table 1) or ordered from commercial suppliers (marked with "(C)" in Table 1). The component structure of the synthesized BCAs is detected and confirmed by means of 1 H NMR and 13  Tetraethylammoniumbromide,

Stabiltiy of Two-Phase Electrolytes and Bromine Binding Strength of BCAs
A total of 38 BCAs are synthesized for this work (marked with "(S)" in Table 1) or ordered from commercial suppliers (marked with "(C)" in Table 1). The component structure of the synthesized BCAs is detected and confirmed by means of 1 H NMR and 13  Tetraethylammoniumbromide,

Stabiltiy of Two-Phase Electrolytes and Bromine Binding Strength of BCAs
A total of 38 BCAs are synthesized for this work (marked with "(S)" in Table 1) or ordered from commercial suppliers (marked with "(C)" in Table 1). The component structure of the synthesized BCAs is detected and confirmed by means of 1 H NMR and 13  Tetraethylammoniumbromide,

Stabiltiy of Two-Phase Electrolytes and Bromine Binding Strength of BCAs
A total of 38 BCAs are synthesized for this work (marked with "(S)" in Table 1) or ordered from commercial suppliers (marked with "(C)" in Table 1). The component structure of the synthesized BCAs is detected and confirmed by means of 1 H NMR and 13

Stabiltiy of Two-Phase Electrolytes and Bromine Binding Strength of BCAs
A total of 38 BCAs are synthesized for this work (marked with "(S)" in Table 1) or ordered from commercial suppliers (marked with "(C)" in Table 1). The component structure of the synthesized BCAs is detected and confirmed by means of 1 H NMR and 13 C NMR. NMR results of all synthesized components are available in the SM (Section 2) and are verified on the basis of NMR results from the literature [45][46][47][48][49][50][51].

. Solubility of [BCA]-Salts in Aqueous HBr Solutions
For their application on the H 2 /Br 2 -RFB, the bromide or chloride salts of the BCAs (Table 1) Figure S1 in the SM.
On the basis of our studies, we assume that the electron-donating inductive effect (+Ieffect) influences the observed trend in Figure 2. The +I-effect increases with rising alkyl side chain length towards the nitrogen atom of the quaternary ammonium and leads to higher bromine binding strength with longer alkyl side chain BCAs and lower [BCA]Br2n+1 solubility in the aqueous electrolyte. In detail, due to the +I-effect, the polarity of the N On the basis of our studies, we assume that the electron-donating inductive effect (+I-effect) influences the observed trend in Figure 2. The +I-effect increases with rising alkyl side chain length towards the nitrogen atom of the quaternary ammonium and leads to higher bromine binding strength with longer alkyl side chain BCAs and lower [BCA]Br 2n+1 solubility in the aqueous electrolyte. In detail, due to the +I-effect, the polarity of the N atom is reduced, making the atom increasingly nonpolar and less soluble in the polar HBr/H 2 O environment as the chain length is increased. In these cases, stronger interactions with the polybromides might be given, while, due to reduced polarity, the interaction with Br 3 − , Br 5 − and Br 7 − is preferred compared to polar Br − ions. To further explain the differences in bromine complexation with increased chain length, in particular on Nheterocycles, former studies on bromine interaction with quaternary ammonium ions can be considered. Easton et al. [17], for example, have calculated the interaction of Br 3 − and Br 5 − with different BCAs by DFT calculation and simultaneously determined the influence of polybromides on the hydrogen atoms in the region around the nitrogen atom in the BCA by 1 H NMR spectroscopy. The protons in the α-positions of pyridinium, piperidinium and pyrrolidinium rings interact most intensively with the polybromide anion [17], which has also been shown by Lungwitz [42].
In conclusion, organic BCA cations with a high symmetry in structure and short alkyl side chains tend to crystallize in contact with polybromides, while BCAs with long alkyl side chains and/or an unsymmetrical BCA structure stay liquid when forming a fused salt with polybromides.

Polybromide Species in [BCA]Br2n+1 Crystals
Beside the structure of BCAs, polybromides are found in the crystals. It raises the question of whether individual polybromides have a decisive influence on the tendency to crystallize with BCA cations. To investigate the reason behind the crystallization, Raman spectra of dry crystals are studied and are shown in Figure S2  The Raman spectra of all show the same distinct features: a very strong peak in the Raman spectrum at a Raman shift (ṽ) between ṽ = 158-167 cm −1 and a weak peak at ṽ = 180-200 cm −1 , which is an adjacent shoulder of the strong peak. An example of the Raman spectrum of [C2MIm]Br3 is shown in Figure 3a. Both peaks are characteristic for tribromide ions Br3 − due to its symmetrical (ṽ = 163 cm −1 ) and antisymmetrical (ṽ = 198 cm −1 ) stretching vibration known from [56][57][58]. The absence of water's characteristic Raman bands, such as ṽ = 1600 cm −1 and between ṽ = 3000 cm −1 and 3800 cm −1 [59][60][61][62], ensures that dry crystals have been studied. Peaks of higher polybromides Raman shifts normally appear at ṽ = 210 cm −1 (Br5 − , antisymmetric stretching vibration), ṽ = 253 cm −1 (Br5 − , symmetric stretching vibration) and ṽ = 270 cm −1 (Br7 − , symmetric stretching vibration) according to Chen et al. [56] but are not detected during the investigation of crystals. Higher polybromides, e.g., Br5 − or Br7 − are not present in the crystals.
However, higher polybromides seem to be bound in the liquid fused salts. The spectra of [C3MIm]Br2n+1, [C4MIm]Br2n+1 and [C6MIm]Br2n+1 are shown in Figure 3b, where the presence of pentabromide and probably heptabromide is evidenced by the appearance of a peak at ṽ = 255 cm −1 . Figure 3b also shows an increase in peak intensity at ṽ = 160 cm −1 (Br3 − ) with increasing alkyl side chain length of the BCA, whereas the identified peak at ṽ  Figure 3b, where the presence of pentabromide and probably heptabromide is evidenced by the appearance of a peak atṽ = 255 cm −1 . Figure 3b also shows an increase in peak intensity atṽ = 160 cm −1 (Br 3 − ) with increasing alkyl side chain length of the BCA, whereas the identified peak atṽ = 255 cm −1 (Br 5 − /Br 7 − ) remains constant. In general, the Raman peak shifts of the crystal samples are similar to those of the fused salts [58]. With an increasing side chain length at an SoC of 33%, bromine is preferentially added as Br 3 − ions. This means that BCAs with longer side chains preferentially form a fused salt in which Br 3 − acts as the counter ion to the [BCA] + cation, but does not crystallize due to steric hindrance from the long alkyl side chain. On the other hand, fused salts formed from BCAs with short alkyl side chains are stable liquid phases when, due to a mixture of Br 3 − , Br 5 − and Br 7 − , the fraction of higher polybromides increases in comparison to Br 3 − . In this case, the steric hindrance of the polybromides and charge distribution prevents the formation of crystals. The distribution of Br 2 in the polybromides depends on the BCA and the specific interactions between BCA and the polybromides. Haller et al. [63] assume that higher polybromides are less strongly bound by BCAs than lower polybromides or bromide ions.
In summary, symmetric and small BCAs tend to crystallize at room temperature with Br 3 − ions because of their higher charge density and lower steric hindrance. Both long side chains of heteroaromatic BCAs and large polybromides do not crystallize at room temperature due to steric hindrance. An exception is [C2Py]Br, which also remains liquid at room temperature.
For further consideration and application, therefore, N-alkylated pyridine-1-ium compounds and 1-alkylated 3-methylimidazol-1-ium compounds are of particular interest. With the alkyl side chains ethyl, n-propyl, n-butyl and n-hexyl, they all exhibit a bromine binding strength of more than 80 mol% at an SoC of 33% resulting in a reduced vapor pressure in the aqueous electrolyte solution. In order to compare their properties with wellinvestigated BCAs such as [C2MP]Br and [C2MM]Br, these two BCA groups are included in further experiments. In this first analysis, the focus has been set on the electrolyte mixture of 1:1 ratio of Br 2 to BCA at an SoC of 33%. However, electrolytes at an SoC of 33% only provide a selective insight into the electrolyte system of a flow battery. In the following, the properties of the electrolytes are examined over the entire capacity range as a function of the SoC.

Stability of Liquid Fused Salts within the Whole SoC Range
In the first preselection process, mainly heteroaromatic 1-alkylpyridin-1-ium and 1-alkyl-3-methylimidazole-1-ium bromides showed stable liquid fused salt phases at room temperature. This has been investigated for a fixed electrolyte mixture of 1. 11

Bromine Binding Strength of [BCA] + (aq) Cations as a Function of the State of Charge (SoC)
The bromine binding strength of the individual BCAs has been determined based on the concentration c(Br 2 ) in the aqueous electrolyte solution compared to the total Br 2 concentration at an SoC of 33% for the 35 chosen BCAs in Figure 5. Now, the change of the [BCA] + concentration over the SoC range will be considered to investigate its effect towards the solubility and bromine binding properties for the seven BCAs based on 1-alkyl-1-pyridin-1-ium bromides and the 1-alkyl-3-methylimidazol-1-ium bromides. For the measurement of the BCA concentration in aqueous solution, the intensity of the characteristic peaks with corresponding Raman shifts is investigated. The Raman shifts of the [BCA] + cations in aqueous solution are listed in Table 2. The Raman peaks selected for the evaluation have certain Raman shifts, which are highlighted in Table 2 in bold. The designated Raman shifts for the investigated BCAs are in agreement with the literature [64]. Concentrations of [BCA] + cations in the aqueous phase are shown in Figure 5.  Br), and indicates their usable SoC range for θ = 23 ± 1 °C.          (Table 2).

Bromine Binding Strength of [BCA] + (aq) Cations as a Function of the State of Charge (SoC)
The bromine binding strength of the individual BCAs has been determined based on the concentration c(Br2) in the aqueous electrolyte solution compared to the total Br2 concentration at an SoC of 33% for the 35 chosen BCAs in Figure 5. Now, the change of the [BCA] + concentration over the SoC range will be considered to investigate its effect towards the solubility and bromine binding properties for the seven BCAs based on 1-alkyl-1-pyridin-1-ium bromides and the 1-alkyl-3-methylimidazol-1-ium bromides. For the measurement of the BCA concentration in aqueous solution, the intensity of the characteristic peaks with corresponding Raman shifts is investigated. The Raman shifts of the  10, 20, 30, 33, 40, 50, 60, 66, 70, 80, Figure 5.  Table S1.
When the BCA is added to the polybromide solution the solubility equilibrium leads to a separation of [BCA]Br2n+1 salts by forming a fused salt phase according to Equation 3, Table S1.
When the BCA is added to the polybromide solution the solubility equilibrium leads to a separation of [BCA]Br 2n+1 salts by forming a fused salt phase according to Equation is present, which decreases for all BCAs at SoC > 0%. Especially for 3-methylimidazol-1-ium derivatives, a linear and BCA-independent decrease in the [BCA] + concentration between 0 ≤ SoC ≤ 20% can be observed (Figure 5b). For pyridin-1-ium derivatives, the same trend is observed between 0 ≤ SoC ≤ 10% in Figure 5a. Between 20 < SoC < 66%, the concentration of BCA continues to decrease for both groups of substances, although these changes become smaller as the SoC increases. In this range, the different bromine binding strength and solubility of the [BCA] [BCA]Br 2n+1 in the aqueous electrolyte for the 1-alkylpyridine-1-ium polybromides and for the 1-alkyl-3-methylimidazole-1-ium polybromides decreases with an increasing length of the alkyl side chain. The detection limits of [BCA] + cations in Table 3 show that 1-alkyl-3-methylimidazol-1-ium is a slightly stronger bromine binding BCA than 1-alkylpyridin-1-ium if both have the same alkyl group in the N-position. As mentioned earlier, the bromine binding strength cannot be the only criteria to choose a BCA. Moderate Br 2 concentrations in the aqueous phase along the whole SoC range are a prerequisite for the operability of the cell and will be investigated in the next section.

Effect of the Solubility Equilibrium on the Br2(aq) Concentration for the Whole SoC Range
Br2 is transported from the tank into the RFB half cell as an ingredient of the aqueous solution. Moderate Br2 concentrations dissolved as polybromide ions in the aqueous electrolyte phase are a prerequisite for stable cell operation. The bromine concentrations in the aqueous phase of the electrolytes for the investigated BCAs are plotted as a function of the SoC in Figure 6.  Table S2. Section I shows a strong dependence of the Br 2 concentration in the aqueous phase on the alkyl side chain length of the BCA, while in section II the Br 2 concentration is independent of the alkyl side chain length. The total Br 2 concentration in the samples allows a direct comparison of the Br 2 concentration in the sample and the aqueous phase for 10 ≤ SoC ≤ 100%.

General Influence of BCA Application on Br 2 Concentration in Aqueous Solution
Due to the relatively low solubility of the BCA-polybromide salt, the Br 2 concentration in the aqueous solution in equilibrium is low compared to the global concentration of Br 2 indicated by the absolute concentration in Figure 6. While the total concentration of Br 2 varies linearly along the SoC range, between c(Br 2 (total)) = 0.35 M at an SoC of 10% and c(Br 2 (total)) = 3.35 M at an SoC of 100% (Figure 6), the solubility equilibrium of the BCAs with the polybromides results in a significantly lower concentration of bromine (c(Br 2 (aq)) < 0.35 M) in the entire SoC range for all investigated BCAs. In addition, no linear relationship between c(Br 2 (aq)) and the SoC is observed. The maximum ratio of Br 2 in the aqueous phase compared to the total Br 2 concentration is present for SoC > 80% and is shown in Table 3/line 2. A maximum fraction of 11 mol% Br 2 is present in the aqueous solution, while a fraction of more than 89 mol% Br 2 is present in the fused salt phase. Although vapor pressures are not measured in this work, the safety of the electrolytes increases tremendously due to the low Br 2 concentrations and the resulting reduced outgassing of Br 2 from the aqueous electrolyte. Additionally, low concentrations of c(Br 2 (aq)) would decrease the available bromine that can crossover across the membrane to the H 2 electrode inside the battery.

Individual Concentration Trends of Different [BCA] + Cations
For BCAs based on 1-alkylpyridin-1-ium and 1-alkyl-3-methylimidazol-ium, characteristic concentration curves for c(Br 2 (aq)) are obtained, whereby both diagrams in Figure 6 can be divided into two sections: In the first section (section I), between 0 < SoC ≤ 40% the Br 2 concentrations in the aqueous solution are different for each BCA but are approximately independent of SoC and are also listed for an SoC of 30% in Table 3, on line 3. One exception is the trend of [C2MIm]Br, which will be explained later. There is a clear trend in Br 2 concentrations in the aqueous phase at an SoC of 30% for the applied BCAs, which corresponds to the trend of BCA- The alkyl side chain length in the N-position in all BCAs is responsible for the differences in complexing strength, which is just a handy indicator for the solubility of the [BCA]Br 2n+1 . The longer the side chain, the lower the solubility of the [BCA]Br 2n+1 in the aqueous solution. Another finding is that in general, the 1-alkyl-3-methylimidazol-1-ium compounds are slightly stronger BCAs compared to the 1-alkylpyridin-1-ium, when the same alkyl side chains are introduced. The concentrations of Br 2 and [BCA] + cations in the aqueous solution both show the same trend.
For the Br 2 concentrations of [C2MIm]Br between 10 ≤ SoC ≤ 50%, there is a concentration plateau in Figure 6b which differs from the c(Br 2 (aq)) curves for [C3MIm]Br, [C4MIm]Br and [C6MIm]Br. As mentioned above, the second phase of [C2MIm]Br is crystalline and consists solely of the tribromide compound ([C2MIm]Br 3 ). Consequently, the ratio of bromine to BCA cation is fixed to 1:1, and no higher polybromides can be stored in the second heavy phase. This leads to rising Br 2 concentrations in the aqueous phase until the second phase liquefies again at SoC ≥ 50%, as presented in Figure 4.
The second section in Figure 6a,b starts from SoC > 40% (section II). Here the Br 2 concentration increases noticeably for all BCAs, whereby the dependence of the Br 2 concentration on the choice of the [BCA] + cation decreases with increasing SoC. For both 1-alkylpyridin-1-ium and 1-alkyl-3-methylimidazolium cations as BCAs, the Br 2 concentration for SoC ≥ 60% increases, whereby for each SoC value examined, approximately equal concentrations c(Br 2 (aq)) are present in the aqueous solution. In this section, the length of the alkyl side chain at the N-position of the BCA seems to have no influence on the binding strength of Br 2 of the second phase in solution. However, 1-alkylpyridin-1-ium bromides bind bromine in section II slightly more strongly and tend to have a lower solubility in the presence of polybromides at SoC > 60% as slightly lower Br 2 concentrations in the aqueous phase are present ( Figure 6). In general, for SoC ≥ 80% the Br 2 concentrations rise only slowly or form a plateau. In that range, the solubility of Br 2 in the aqueous solution is limited by a lack of bromide ions to form polybromides, known from BCA-free electrolytes [65].
It is noticeable over the whole range that for small amounts of Br 2 at SoC ≤ 40%, the complexation strength of the individual BCA types has a major influence on bromine concentration in the aqueous phase, but at SoC ≥ 60% neither the type of BCA base nor the length of the alkyl side chain seem to play a noticeable role, where all BCAs are considered to complex polybromides to a similar extent. At the same time, there is a transfer of Br 2 from the aqueous phase into the fused salt over the entire SoC range, but since it has been shown above that no BCA cations are present in the aqueous solution at higher SoCs, the transfer no longer occurs according to Equation (3).

Theoretical Comparison of Br 2 Concentrations and Current Densities in the H 2 /Br 2 -RFB Cell
Overall, the concentrations of c(Br 2 (aq)) are concentrations of Br 2 in chemical equilibrium for both phases and are only present during operation if the mass transfer of Br 2 from the fused salt to the aqueous electrolyte phase takes place without any mass transfer limitation, i.e., the equilibrium state is maintained during the discharge process. Applying this theoretical assumption, the current densities of i = 723 mA cm −2 for c (Br 2 Figure 2, they seem to be more applicable for effective cell operation. From Figure 6 it is noticed that in the range of an SoC of 33%, Br 2 concentrations in the aqueous solutions are lowest. For the protonated forms it is therefore expected that for higher SoCs, much larger Br 2 concentrations are present and electrolytes cannot still be classified as "safe" electrolytes. From the results in this section, it is expected that concentrations might rise for a higher SoC and lead to greater volatility of Br 2 .
[C2Py]Br tends to be the [BCA] of choice in order to reach performance and safety of the Br 2 /Br − electrolytes.

Distribution of Br 2 on Polybromides in the Aqueous Phase
As presented in the previous section, the aqueous Br 2 concentration defines the power capability of the cell. For a deeper understanding of the complexation behavior of the different BCAs, the Raman spectra of the aqueous phase have been analyzed regarding the distribution of bromine in the different polybromides. The method has been described in our earlier work [65]. The distribution of Br 2 on Br 3 − , Br 5 − and Br 7 − is shown in Figure 7. The Raman spectra of all investigated samples are shown in the SM in Figures S3-S9. ing the distribution of bromine in the different polybromides. The method has been described in our earlier work [65]. The distribution of Br2 on Br3 -, Br5 -and Br7 -is shown in Figure 7. The Raman spectra of all investigated samples are shown in the SM in Figure S3 to S9. An analysis of the distribution of Br2 among the polybromides Br3 − , Br5 − and Br7 − in the aqueous phase shows basically similar results for both BCA groups as shown in Figure  7a,b. For all investigated BCAs, the storage of Br2 in the aqueous electrolyte in the form of Br5 -predominates, followed by storage in Br3 -and finally storage in Br7 − . This is in accordance with earlier studies on pure BCA-free HBr/Br2/H2O-electrolytes [65], leading to the result that [BCA] + has only a minor influence on the fractions of Br2 in the different polybromide species in the aqueous solution. For SoC < 40%, the n-hexyl side chain BCAs [C6Py]Br and [C6MIm]Br have a slightly increased Br2 content in Br3 − , which means that less Br2 is distributed to the Br5 − and Br7 − anions. For SoC < 40%, n-butyl, n-propyl and ethyl BCAs have a constant Br2 distribution, which is independent of the BCA. For BCAs alkylated with an n-hexyl group, more Br3 − is available, while less Br2 is stored in Br5 -and Br7 − . In this range, cations of [C6Py] + and [C6MIm] + are available in the aqueous solution and already prefer to interact with Br3 -in comparison to Br5 -and Br7 − . This is in accordance with the composition of their fused salt phases, shown in Figure 3b. For an SoC of ≥ 40%, there is no dependence of the Br2 distribution in the aqueous phase on the length of the alkyl radical present in the N-position of the BCA. The distribution is independent of the choice of the BCA basic compound pyridine or 3-methylimidazole. Within this SoC range, the fraction of Br2 stored as Br3 -increases from 30.7% to 41.6−47.3%, while proportionally less Br2 is stored in Br5 − and the curve decreases from 60% to 46-50%. Br2 remains in Br7 − within the whole SoC range relatively constant up to a maximum of 13.5%. Presumably, a better solvation of the more stable Br3 − compared to Br5 -is present. This effect is obtained also for BCA-free HBr/Br2/Brsolutions [65]. Since the Br2 concentration of c(Br2(aq)) < 0.35 M and the distribution of Br2 to the polybromides is  − . This is in accordance with the composition of their fused salt phases, shown in Figure 3b.
For an SoC of ≥ 40%, there is no dependence of the Br 2 distribution in the aqueous phase on the length of the alkyl radical present in the N-position of the BCA. The distribution is independent of the choice of the BCA basic compound pyridine or 3methylimidazole. Within this SoC range, the fraction of Br 2 stored as Br 3 − increases from 30.7% to 41.6−47.3%, while proportionally less Br 2 is stored in Br 5 − and the curve decreases from 60% to 46-50%. Br 2 remains in Br 7 − within the whole SoC range relatively constant up to a maximum of 13.5%. Presumably, a better solvation of the more stable Br 3 − compared to Br 5 − is present. This effect is obtained also for BCA-free HBr/Br 2 /Br − solutions [65]. Since the Br 2 concentration of c(Br 2 (aq)) < 0.35 M and the distribution of Br 2 to the polybromides is relatively constant in the whole range, no specific influence of this distribution on the performance or individual parameters is given and therefore cannot be discussed.

Influence of Different BCAs on Electrolyte Conductivity of the Aqueous Phase
For both flow-by and flow-through electrodes in RFBs, a low ohmic cell resistance is required to achieve high cell or stack performance. In RFB, this strongly depends on the electrolyte composition at different SoCs, usually targeting the maximum electrolyte conductivity of the aqueous electrolyte phase. Electrolyte conductivities of the aqueous phases from the seven pre-selected [BCA]/Br 2 electrolytes summarized in Table 2 are shown in Figure 8. In addition, the reference conductivity curves of a BCA-free HBr/Br 2 /H 2 O electrolyte (from [65]) and a pure HBr/H 2 O acid solution within the SoC range are shown in Figure 8 relatively constant in the whole range, no specific influence of this distribution on the performance or individual parameters is given and therefore cannot be discussed.

Influence of Different BCAs on Electrolyte Conductivity of the Aqueous Phase
For both flow-by and flow-through electrodes in RFBs, a low ohmic cell resistance is required to achieve high cell or stack performance. In RFB, this strongly depends on the electrolyte composition at different SoCs, usually targeting the maximum electrolyte conductivity of the aqueous electrolyte phase. Electrolyte conductivities of the aqueous phases from the seven pre-selected [BCA]/Br2 electrolytes summarized in Table 2 are shown in Figure 8. In addition, the reference conductivity curves of a BCA-free HBr/Br2/H2O electrolyte (from [65]) and a pure HBr/H2O acid solution within the SoC range are shown in Figure 8. All measured values are listed in Table S6 and S7 in the SM. The values for pure HBr/H2O acid at θ = 20 °C are calculated from molar conductivities from [66] and are adapted to the SoC scale. Electrolytic conductivities in the aqueous phase depend mainly on the high proton concentration and are larger than 300 mS cm −1 throughout the SoC range, whereby the Grotthus mechanism [67,68] is responsible for ionic transport through the solution. In this chain-hopping mechanism, bonds are attached and released between water and protons in oxonium ions. Ionic transport by the vehicle mechanism [67] is subordinated to the Grotthus mechanism in aqueous electrolyte solutions. With conductivities between 324.8 ≤ κ ≤ 745.0 mS cm −1 , all aqueous electrolytes containing BCAs have large electrolyte conductivities and are feasible for application in the H2/Br2-RFB. Electrolytic conductivities in the aqueous phase depend mainly on the high proton concentration and are larger than 300 mS cm −1 throughout the SoC range, whereby the Grotthus mechanism [67,68] is responsible for ionic transport through the solution. In this chain-hopping mechanism, bonds are attached and released between water and protons in oxonium ions. Ionic transport by the vehicle mechanism [67] is subordinated to the Grotthus mechanism in aqueous electrolyte solutions. With conductivities between 324.8 ≤ κ ≤ 745.0 mS cm −1 , all aqueous electrolytes containing BCAs have large electrolyte conductivities and are feasible for application in the H 2 /Br 2 -RFB.
The [BCA] + cations in the electrolyte mixture influence the electrolyte conductivity within the entire SoC range compared to BCA-free HBr/Br 2 /H 2 O electrolytes, as shown in Figure 8. For 0 ≤ SoC ≤ 60% for both 1-alkylpyridin-1-ium electrolytes and for 1-alkyl-3methylimidazol-1-ium electrolytes, κ rises approximately from 368.90 to 478.00 mS cm −1 at an SoC of 0% to reach a peak at κ = 643.1−681.84 mS cm −1 between an SoC of 50 and 60%. Within this range, there is a difference from the two reference curves in accordance with the concentrations of the [BCA] + cation in solution, shown in Figure 5. Initially, the organic character of [BCA] + cation decreases the conductivity. Organic [BCA] + cations with longer alkyl side chains lead to lower conductivity in the aqueous phase due to their increasing size. On the one hand, their migration in the electric field is slowed down and the ionic transport by the Grotthus mechanism is restricted. Grotthus charge transfer on a direct path between the electrodes is hindered and is forced to bypass the large organic cations. However, as the SoC is increased, the conductivity of the aqueous electrolyte in Figure 8 is shown to increase. This observation can be directly related to the results presented in Figure 5, whereby the [BCA] + concentration of the investigated BCAs in the aqueous electrolyte is shown to decrease with the SoC as an indication that the cations are now bonded to the fused salt phase and leaving the aqueous electrolyte phase. Thus, based on these results, the decrease in the aqueous electrolyte [BCA] + concentration translates into the increased electrolyte conductivity trend seen in Figure 8 between 0 ≤ SoC ≤ 60%.
For electrolytes with 1-alkylpyridin-1-ium bromide as a BCA, the complexation strength with respect to the side chain can be read in Figure 8a. Since [C6Py] + with polybromides Br 2n+1 − is less soluble in the aqueous phase than [C2Py] + , their concentration decreases more rapidly compared to [C2Py] + . The conductivity of the solution increases correspondingly more quickly in Figure 8a compared to electrolytes containing [C4Py] + or [C2Py] + .
In the second range for 60 < SoC ≤ 100%, there are hardly any [BCA] + cations available in the aqueous phase, as presented in Section 2.3. In this range, no direct dependence of conductivity on the alkyl side chain in the N-position of the [BCA] + cation is obtained. Electrolytes with BCAs show approximately same conductivities. With an increasing SoC, the proton concentration decreases, and the conductivity of the solution decreases subsequently.
However, electrolytes containing BCAs reach higher conductivities compared to BCAfree HBr/Br 2 /H 2 O electrolytes for SoC ≥ 50% (green dots, in Figure 8). Due to the transfer of Br 2 by use of the BCA from the aqueous phase into the fused salt, only concentrations lower than 0.35 M Br 2 compared to the maximum total concentration of 2.99 M Br 2 in BCA-free HBr/Br 2 /H 2 O electrolyte (calculated from values in [65]) are present in aqueous electrolytes. Since the absolute Br 2 concentration in the aqueous electrolytes with BCA is much lower, while the concentration of protons in both solutions is assumed to be the same, the conductivity is higher when using BCAs and is comparable to pure HBr/H 2 O solutions as shown in Figure 8. The Grotthus mechanism takes place directly between the electrodes and does not need to bypass larger polybromides, as is the case in BCA-free HBr/Br 2 /H 2 O electrolytes [65]. As for SoCs > 60%, the [BCA] + cations are not available in the aqueous phase; the conductivity of the resulting electrolytes in that range is shown to be higher than in BCA-free HBr/Br 2 /H 2 O electrolytes.
In this work, the achieved conductivities correspond to those of a pure HBr/H 2 O solution, which for an SoC of ≥ 60% means an increase in conductivity compared to HBr/Br 2 /H 2 O electrolytes and has a positive effect on cell performance. These high conductivities are due to the presence of the high proton concentration of c(HBr) ≥ 1 M. The influence of BCAs is directly attributable to the presence of BCAs for an SoC of < 60% and indirectly for an SoC of ≥ 60%. These high conductivities allow one to obtain high current densities at a low expected electrolyte overvoltage, depending on the half-cell structure.
In Equation (4), F is the Faraday constant (96485 As mol −1 ), R the molar gas constant (8.3145 J mol −1 K −1 ) and T the temperature in K. ϕ 0 (Br 2 |Br − ) is the standard redox potential of the Br 2 /Br − electrolyte with 1.09 V [9]. The theoretical potential curve following the Nernst equation (Equation (4)) and global concentrations of HBr and Br 2 at T = 298.15 K are applied. The curve is shown in Figure 9 as a function of the SoC (orange line). It has much higher values at corresponding SoCs compared to the measured redox potential of BCA-free electrolytes in Figure 9 (green dots). In the electrolyte system under investigation, there are no ideally diluted solutions, but strongly concentrated electrolytes. As a result, redox potentials according to the NERNST equation must be considered including activity coefficients as shown in Equation (5)  For low SoCs with high concentrations c(HBr) > 1.2 M of HBr, the activity coefficients for γ(HBr) > 1 are available (calculated with data from [71]). Increasingly higher activities a(HBr) = c(HBr) γ(HBr) must be taken into account in the calculation of the redox potential of the positive half cell due to constantly increasing activity coefficients of HBr in the aqueous solution [71]. Wlodarczyk et al. [70] clearly show that the increasing activity coefficients of HBr for low SoCs leads to a strong decrease in the redox potential of the bromine electrolyte at an electrode according to Nernst compared to a pure concentrationbased calculation.
The measured redox potential ϕ(Br 2 /Br − ) of the pure HBr/Br 2 /H 2 O electrolytes (green curve in Figure 9) increases with an increasing SoC from 0.76 V vs. NHE (at an SoC of 0%) and a maximum value at an SoC of 100% at 1.12 V vs. NHE. For SoC ≥ 89.4%, Br 2 is not completely soluble in the aqueous solution as explained in [65]. The aqueous solutions contain less Br 2 , and the redox potential flattens following the Nernst equation (Equation (5)).
there are no ideally diluted solutions, but strongly concentrated electrolytes. As a result, redox potentials according to the NERNST equation must be considered including activity coefficients as shown in Equation 5 [70]: φ(Br2|Br − ) = φ 0 (Br2|Br − ) -0.5 R T F −1 ln(c(Br − ) 2 (Br − ) 2 c(Br2) −1 (Br2) −1 ) (a) (b) Figure 9. Redox potentials of the redox couple Br -/Br2 in aqueous posolyte vs. NHE as a function of its state of charge SoC measured on a glassy carbon electrode without [BCA]Br and with (a) 1-alkylpyridine-1-ium bromides and (b) 1-alkyl-3methylimidazole-1-ium bromides as BCAs with different alkyl side chain groups in the N-position of the BCA at θ = 23 ± 1 °C. The orange line shows the simulated redox potential following the Nernst equation and is based on global concentrations of HBr and Br2. The measured redox potential of BCA-free HBr/Br2 electrolytes is shown with green dots for comparison and was first published in [70]. Values of redox potentials of the electrolytes containing BCAs are printed in the SM of this study in Table S8.
For low SoCs with high concentrations c(HBr) > 1.2 M of HBr, the activity coefficients for γ(HBr) > 1 are available (calculated with data from [71]). Increasingly higher activities a(HBr) = c(HBr) γ(HBr) must be taken into account in the calculation of the redox potential of the positive half cell due to constantly increasing activity coefficients of HBr in the aqueous solution [71]. Wlodarczyk et al. [70] clearly show that the increasing activity co- Figure 9. Redox potentials of the redox couple Br − /Br 2 in aqueous posolyte vs. NHE as a function of its state of charge SoC measured on a glassy carbon electrode without [BCA]Br and with (a) 1-alkylpyridine-1-ium bromides and (b) 1alkyl-3-methylimidazole-1-ium bromides as BCAs with different alkyl side chain groups in the N-position of the BCA at θ = 23 ± 1 • C. The orange line shows the simulated redox potential following the Nernst equation and is based on global concentrations of HBr and Br 2 . The measured redox potential of BCA-free HBr/Br 2 electrolytes is shown with green dots for comparison and was first published in [70]. Values of redox potentials of the electrolytes containing BCAs are printed in the SM of this study in Table S8. In principle, the redox potential of the aqueous electrolyte solution with the use of [BCA]Br in the presence of Br 2 is lower within the entire SoC range compared to BCA-free HBr/Br 2 /H 2 O electrolytes ( Figure 9). The transfer of Br 2 into the fused salt reduces the bromine concentration in the aqueous solution, while at the same time the HBr concentrations stay nearly constant in comparison to BCA-free HBr/Br 2 /H 2 O electrolytes. Hence, according to Equation (4), the redox potential of [BCA]Br electrolytes is slightly lower when compared to the BCA-free HBr/Br 2 /H 2 O electrolytes. For SoCs < 50%, the solubility of the respective [BCA] + cation is responsible for the trend observed in Figure 9. In accordance with lower bromine concentrations in the electrolyte for increasing the n-alkyl side chain length ( Figure 6), lower redox potentials are observed with the BCA electrolytes with larger n-alkyl chain. For SoCs > 50%, the difference between the potentials of the pure HBr/Br 2 /H 2 O electrolyte and the electrolytes containing BCA becomes increasingly larger. In global terms, the Br 2 concentration increases strongly, which can be seen in the potential of the BCA-free HBr/Br 2 /H 2 O electrolyte, but at the same time the majority of the Br 2 in the solutions with BCAs is transferred to the fused salt. The redox potentials of the electrolytes with BCAs increase at a slower rate with an increasing SoC.
The use of [BCA]Br leads to an average reduction in the redox potential of the positive half cell and the cell voltage ∆E by 32 ≤ ∆E ≤ 114 mV for all BCAs and over the entire SoC range compared to pure HBr/Br 2 /H 2 O electrolytes. The performance of the cell is reduced by this effect, while it is already lowered by high activity coefficients of HBr [70,71]. Fabjan et al. [8] described for Zn/Br 2 -RFB electrolytes that solutions of [C2MM]Br and [C2MP]Br reduce the concentration of Br 2 in the aqueous phase to approximately 0.01 M, and the redox potential is characteristically reduced by 50 to 70 mV. This applies to our electrolytes and both BCA series in Figure 9 for the range 30 ≤ SoC ≤ 70%. A lower cell voltage due to the use of BCAs must be accepted as a trade-off for limiting the Br 2 concentration in the aqueous solution.

Interpretation of the Study and Selection of a Promising BCA for Application in Cell Tests
In the scope of this research, 38 cost-effective BCAs have been investigated and evaluated on the basis of their solubility, Br 2 binding strength, ionic conductivity and equilibrium potential for their possible application as electrolytes on H 2 /Br 2 -RFBs. In the following, an elimination procedure is applied to select the most suitable BCA for battery operation. The BCAs are excluded on the basis of the results obtained in the previous sections. To start, based on their solubility, [ Br form solid crystals in the aqueous solution instead of a liquid fused salt when they come into contact with polybromides. Hence, none of these BCAs can be used in the cell as the spontaneous formation of crystals in the cell, tubing and pumps can lead to operational problems.
Since the H 2 /Br 2 RFB is intended to be operated at high current densities due to the good reaction kinetics of both electrode reactions, a high mass flow of Br 2 into the cell during the discharge reaction is necessary, making high concentrations of Br 2 desirable. At the same time, it is the task of the BCAs to reduce the bromine concentration in the aqueous phase in order to increase safety. All BCAs that form a liquid fused salt phase and have long alkyl side chains such as n-butyl or n-hexyl have a bromine binding strength of >95 mol%. Additionally, all BCAs with a liquid fused salt phase and ethyl or n-propyl as a side chain, with the exception of [C2Py]Br, have a bromine binding strength of >90 mol%. These BCAs do not leave sufficient Br 2 in the aqueous phase of the electrolyte to achieve acceptable current densities. The availability of Br 2 in the liquid electrolyte phase turned out to be a decisive factor in our selection, making this compound clearly stand out over all the other investigated BCAs. The initial cycling tests and investigation of the [C2Py] + cations on the cell performance during the charge and discharge operation are shown in parallel in [72].

Materials and Methods
A detailed description of the testing methods is given in the SM (Section 1) for this article to enable reproducibility of the measurements. An abbreviated form is reproduced here.

Reagents
Reagents used for preparation of bromine electrolyte samples in this work are hydrobromic acid, bromine and distilled water. Chemicals for the synthesis of BCAs are named in the Supplementary Materials (SM) including suppliers and purities.

Synthesis of Bromine Complexing Agents
The investigated BCAs are listed in Table 1

Redox Potential of the Electrolytes
The redox potentials of the aqueous electrolyte solution are investigated on a glassy carbon stick electrode vs. an Ag/AgCl/KCl(sat.) reference electrode at θ = 23 ± 1 • C and corrected to present them vs. a normal hydrogen electrode. A detailed description can be found in the ESI.

Conclusions
In this study, tertiary ammonium compounds of pyridine, pyrrolidine, morpholine, 3-methylimidazole, tetraalkylammonium and picolines have been alkylated with n-alkyl side chains in the N-position to form organic bromide or chloride salts. In combination with some commercially available organic salts, this resulted in 38 organic quaternary ammonium substances from these six N-containing building blocks. The substances have been investigated ex situ on their properties as BCAs in HBr/Br 2 -electrolytes: BCA solubility, Br 2 binding strength, the stability of the second heavy fused salt phase, Br 2 concentration for application, electrolyte conductivity and redox potential. This study has been performed to define their applicability of BCAs to limit the vapor pressure of Br 2 in aqueous highly concentrated electrolytes for a high-energy density H 2 /Br 2 -RFB with a theoretical capacity of 180 Ah L −1 /196 Wh L −1 (7.7 M HBr).
From the 38 substances evaluated, 15 are not soluble in the electrolyte or form a crystal phase in contact with polybromides. This behavior makes them unsuitable for their application in RFBs. We found that BCAs with short side chains and/or symmetric structure tend to form crystals instead of forming liquid fused salts. An investigation of the [BCA]-polybromide crystal composition showed that all BCA crystals are tribromide salts [BCA]Br 3 .
All the other BCAs form fused salt phases, while most of them exhibit a strong bromine binding strength (14 substances > 95 mol% and four substances between 90 to 95 mol%); four of the N-position protonated BCAs show insufficient binding strengths (<80 mol%).
The binding strength increases with an increase in alkyl side chain length, yet the structure of the six basic components (pyridine, picoline, etc.) only has minor influence on the bromine binding strength in solutions.
1-alkyl-3-methylimidazol-1-ium and 1-alkylpyridin-1-ium bromides have been investigated within the whole SoC range to compare the influence of side chain alkyl groups on the different parameters evaluated throughout this study: For a low SoC (<40%), the selected BCAs show different bromine binding strengths. A clear trend has been found as short alkyl side chains lead to lower Br 2 binding strength compared to those with long alkyl side chains. For an SoC of ≥40%, the concentrations of Br 2 in the electrolyte's aqueous phase increase, while the binding strength becomes independent of the alkylated side chain. However, to obtain a clear insight on the reason behind this behavior, further investigation on the fused salt phase would be needed which is beyond the scope of this study. On a final note regarding this comparison, it is worth mentioning that the ability to form a fused salt phase differed from that of the [C2Py]Br and the [C2MIm]Br BCAs as we observed that while [C2Py]Br forms a liquid fused salt, the cation of [C2MIm]Br tends to crystallize over a wide SoC range.
The ionic conductivity of the aqueous phase is high for the whole SoC range between 325 and 745 mS cm −1 and depends primarily on the available proton concentration and its ionic transport by the Grotthus mechanism. The concentration of [BCA] + in the aqueous phase can, to a lesser extent, influence the measured ionic conductivities of the electrolytes as their presence can slightly reduce the conductivity or increase it indirectly by sequestration of Br 2 from the aqueous phase.
The redox potential of the electrolyte is reduced by 32 to 114 mV due to the use of BCAs compared to BCA-free electrolytes in the whole SoC range. Following the Nernst equation, the decrease in Br 2 concentration in the aqueous phase leads to reduced redox potentials of the half-cell reaction. This is certainly a trade-off that must be accepted as it is a direct consequence of the ambition to lower bromine vapor pressure by limiting Br 2 concentration in aqueous solutions.
Based on the results of fused salt stability over the SOC range, electrolyte conductivity, the trend of the redox potential and especially the concentrations of Br 2 remaining in the aqueous electrolyte phase, one BCA was selected from 38 BCAs and needs to be investigated in detail and applied in the positive half cell of the H 2 /Br 2 -RFB cell: 1-ethylpyridin-1-ium bromide ([C2Py]Br).

Supplementary Materials:
The following are available online: Detailed description of the measurement methods, synthesis of BCAs, manufacturers' data and chemical purities (Chapter S1), as well as 1 H NMR and 13 C NMR interpretation for synthesized BCAs (Chapter S2), tabulation of measured values for Figures within the main manuscript (Table S1-