Literature DB >> 35071879

Facts or Artifacts: Pitfalls in Quantifying Sub-ppm Levels of Ammonia Produced from Electrochemical Nitrogen Reduction.

Suchi Smita Biswas1, Arunava Saha1, Muthusamy Eswaramoorthy1,2.   

Abstract

Synthesis of ammonia through electrochemical nitrogen reduction (ENR) is emerging as one of the attractive research areas in recent years, notwithstanding the enormous challenges it faces in quantification of ammonia at very low concentrations. Several reports claiming high production rate are unwittingly compromised by the accuracy of analyzing a very low concentration (<1 ppm) of ammonia in the electrolyte post-ENR reaction using the indophenol method. Therefore, in this work, we have highlighted the significance of selecting and standardizing a right protocol encompassing admissible levels of oxidants and a complexing agent, citrate (to mitigate the effect of interfering metal ions), through elaborate control experiments. In addition, the importance of setting the lowest limit of ammonia concentration that can be accurately quantified by the indophenol method is also justified. Further, the experimental observations were summarized into a protocol, which was followed to re-evaluate the performance of two well-claimed electrocatalysts for ENR reported recently in the literature.
© 2022 The Authors. Published by American Chemical Society.

Entities:  

Year:  2022        PMID: 35071879      PMCID: PMC8771696          DOI: 10.1021/acsomega.1c05263

Source DB:  PubMed          Journal:  ACS Omega        ISSN: 2470-1343


Introduction

Researchers around the globe are in search of an energy-efficient alternative to the century-old Haber Bosch process for ammonia production. Recent progress made in the generation of electricity from renewable sources generated a great deal of interest in electrochemical ammonia synthesis from nitrogen and water under ambient conditions.[1−4] However, the inert nature (941 kJ/mol bond dissociation energy) and low solubility (20 ppm at 20 °C, 1 atm) of N2 in water coupled with the competing hydrogen evolution reaction are the major challenges for the electrochemical nitrogen reduction (ENR) reaction in an aqueous medium.[5−7] Several reports in recent years claim an ammonia production rate anywhere between 2 and 120 μgNH3 h–1 mgcat–1 using metals, metal oxides, chalcogenides, and carbon as electrocatalysts.[8−13] Nevertheless, it is being realized lately that the isolation of ENR ammonia from contaminants is an insurmountable task to deal with in this reaction. Interference of atmospheric NH3, NO contamination, and the presence of reducible N species in the catalysts are some of the major contributors to the false-positive reports in this field.[14−17] As a natural corollary, many tall claims made in the field of electrochemical nitrogen reduction (ENR) in recent years are obfuscated with these experimental errors and require a revisit. Although there are a few excellent articles that underline the need to adopt careful experimental protocols to eliminate NO and NH3 from the electrochemical system prior to reactions,[15,18,19] in-depth analysis of spectrometric quantification of ammonia by the indophenol method (in an aqueous medium) has been overlooked in this field of research for quite some time. To draw attention to this oversight, we have juxtaposed in Figure the ammonia production rate as reported and the actual concentration of ammonia produced. The concentration of ammonia was extracted from the absorbance maxima value of the ultraviolet–visible (UV–vis) absorption data of the indophenol method provided in some of these reports (details in Table S1). It is evident from Figure that the actual concentration of ammonia produced is below 0.6 ppm for most of the reported catalysts. It also reveals a huge variation in the ammonia production rate even for a small change in the measured concentration. For example, the production rate showed a variation from 0.97 μg h–1 mgcat–1 (for N and P codoped carbon, S.No. 58 in Table S1)[20] to 50 μg h–1 mgcat–1 (for Ru/rGO, S.No. 6 in Table S1)[21] for a concentration difference of 0.02 ppm. Such a large variation for a slight change in concentration actually resulted from the conversion factor (from the concentration to the production rate in μg h–1 mgcat–1 or in some cases μg h–1 cm–2), which involves multiplication of volume of the electrolyte and division by the amount of catalyst used and the reaction time. This conversion factor resulted in reporting a wide range of yields despite similar concentrations, as the volume of electrolyte and the amount of catalyst used varied from one report to the other.
Figure 1

Performance mapping of ENR electrocatalysts from the literature. The reported ammonia production rates of highly explored metal, metal oxide, and carbon-based electrocatalysts are shown in turquoise blue triangles. Very few catalysts with production rate above 80 μg h–1 mgcat–1 are not presented in this graph but included in the reference.[13] The pink circles denote the extracted ammonia concentration from the UV–vis absorption data available for some of the catalysts (Table S1 for calculation details). The horizontal dotted line (pink color) indicates that the concentration of ammonia produced for most of the catalysts lies below 0.6 ppm.

Performance mapping of ENR electrocatalysts from the literature. The reported ammonia production rates of highly explored metal, metal oxide, and carbon-based electrocatalysts are shown in turquoise blue triangles. Very few catalysts with production rate above 80 μg h–1 mgcat–1 are not presented in this graph but included in the reference.[13] The pink circles denote the extracted ammonia concentration from the UV–vis absorption data available for some of the catalysts (Table S1 for calculation details). The horizontal dotted line (pink color) indicates that the concentration of ammonia produced for most of the catalysts lies below 0.6 ppm. It underlines the importance of following stringent protocols to accurately quantify ammonia concentration in the electrolyte. Although isotopic labeling experiments help validate the ammonia production devoid of contaminants,[14,22] the cost and not-so-easy accessibility of 15N2 are some of the limitations to its extensive use. The most widely used technique to quantify ammonia in the aqueous-phase ENR reaction is the well-known indophenol method.[23] Although this is an age-old method, there is no uniformity in the procedures (in terms of the order of addition of reagents, addition of the complexing agent, and the amount of oxidant used) adopted in the literature, and the various protocols used compound the problem of accurate estimation of ammonia[24,25] at sub-ppm-level concentrations in the ENR reaction. In our work, we have highlighted the importance of documenting ammonia produced in terms of “concentration” (in the electrolyte) along with the normalized production rate in the ENR reaction. The significance of selecting and standardizing the right protocol encompassing an admissible level of oxidant and a complexing agent, citrate (to mitigate the effect of interfering metal ions), is discussed elaborately with definitive control experiments. Above all, the efficacy of setting the lowest limit of ammonia concentration that can be accurately quantified by the indophenol method is highlighted in this work. Summarizing our observations, we proposed a standardized protocol that was subjected to verification on the performance of two well-claimed electrocatalysts for ENR reported recently in the literature (Au3Pd/NF and ZnS/NF). The critical analysis addressed here will establish more reliability in quantification and documentation of the amount of ammonia produced from ENR in an aqueous medium.

Experimental Section

Reagents and Materials

Salicylic acid (≥99.0%), sodium hypochlorite (NaClO with available chlorine 4.00–4.99%), sodium nitroferricyanide, sodium citrate, NH4Cl, Ce(NO3)3·6H2O, CrCl3·6H2O, Ni(NO3)2·6H2O, Fe(NO3)3·9H2O, sulfadiazine, N-(1-napthyl)ethylenediamine dihydrochloride, vanadium(III) chloride, HAuCl4, Na2PdCl4, and Zn(Ac)2·2H2O were purchased from Sigma-Aldrich Chemical Co., Ltd. Pluronic F-127, potassium permanganate (KMnO4), sodium sulfate (Na2SO4), and thiourea were obtained from Alfa-aesar. Tetrahydrofuran (THF) (>99.5%), C2H5OH, 25% ammonia solution (NH4OH), H2SO4 (98%), and HCl (37%) were purchased from Merck. Ni foam was procured from Fuel Cell Store.

Characterization and Measurements

X-ray diffraction (XRD) analysis was performed using the Bruker D8 advance eco instrument with a Cu Kα radiation source (λ = 1.54 Å; step size: 0.02; current: 30 mA; and voltage: 40 kV). Field emission scanning electron microscopic (FESEM) images of the samples were obtained via a Nova-Nano SEM-600 (FEI, The Netherlands). UV–vis measurements were performed using the Perkin Elmer Lambda 900 UV–vis instrument.

Synthesis of Au3Pd/Ni Foam (Au3Pd/NF)[26]

A piece of Ni foam (1 cm × 2 cm) was treated with 3 M HCl to remove any oxide layer. Then, it was washed with Milli-Q water and ethanol under sonication and dried in an oven. Au3Pd/NF was synthesized by following the reported procedure. First, Pluronic F-127 (10 mg) was dissolved in THF (3 mL). Then, 1.5 mL of C2H5OH was added to it. To this mixture, 1.5 mL of an aqueous solution of HAuCl4 (20 mM) and 0.5 mL of an aqueous solution of Na2PdCl4 (20 mM) were added. Ni foam (1 cm × 2 cm) was dipped in this solution for 20 min. A visible color change of the solution was observed from golden yellow to colorless (Figure S11a). Au3Pd/NF was obtained after washing with water and drying at an ambient condition at 60 °C.

Synthesis of the ZnS/Ni Foam (ZnS/NF) Catalyst[27]

A piece of Ni foam was pretreated according to the above procedure for removal of any oxide layer. Then, 1 mmol of Zn(Ac)2·2H2O and 3 mmol of thiourea were dissolved in 30 mL of Milli-Q water under continuous stirring. This solution was then transferred to a 50 mL Teflon-lined stainless steel autoclave, and the piece of Ni foam was dipped in it. The autoclave was kept at 160 °C for 6 h. The obtained ZnS/NF (Figure S14a) was washed with a mild acidic solution (0.05 M H2SO4) until excess ammonia was not found in the supernatant of the solution post washing (Figure S15). It was further rinsed with Milli-Q water and absolute ethanol and dried in an oven at 60 °C.

Standardization of the Indophenol Procedure

Among several indophenol methods available in the literature for ammonia quantification in ENR, we have selected four different procedures (labeled as P1, P2, P3, and P4) for quantifying ammonia in blank Milli-Q water and in 0.3 ppm ammonia standard solution (prepared using NH4Cl). Salicylic acid (≥99.0%), sodium hypochlorite (NaClO with available chlorine 4.00–4.99%), and a catalyst, sodium nitroferricyanide, were used as common indophenol reagents in all of the procedures. Only in procedures P1 and P2, sodium citrate was additionally used. Furthermore, the concentration of reagents and their sequence of addition in the analyte are procedure-dependent and are given in Table . One must follow the steps mentioned in Table for each procedure with freshly prepared indophenol reagents. As an example, in procedure P1, first 2 mL of coloring agent (5 wt % salicylic acid and 5 wt % sodium citrate in 1 M NaOH) was added into 2 mL of analyte, followed by addition of 1 mL of an oxidizing agent solution (0.05 M NaClO) and 200 μL of catalyst (1 wt % sodium nitroferricyanide) in sequence. The solution with the analyte and indophenol reagents was mixed thoroughly and stored in the dark (without any light) at room temperature for 2 h. This was followed by a UV–visible absorption measurement (Perkin Elmer Lambda 900) using a 10 mm quartz cuvette to obtain the spectrum with absorption maxima (Aλmax) at 645 nm.
Table 1

Stepwise Procedure for Four Different Indophenol Methods Adopted for Ammonia Quantification in ENRa

procedureanalyte volumestep 1step 2step 3incubation time (h)mole ratio of salicylate: NaClOreferences
P12 mL2 mL (5 wt % salicylic acid, 5 wt % citrate in 1 M NaOH)1 mL (0.05 M NaClO)0.2 mL (1 wt % cat.)21:0.07(16)
P2500 μL500 μL (0.5 M NaClO)50 μL (5 wt % salicylic acid, 5 wt % citrate in 1 M NaOH)10 μL (0.5 wt % cat.)31:14(29)
P34 mL50 μL (0.02 M NaClO in 0.75 M NaOH)50 μL (1 wt % cat.)500 μL (6.4 wt % sodium salicylate in 0.32 M NaOH)11:0.005(26)
P44 mL50 μL (0.75 M NaClO in 0.75 M NaOH)500 μL (6.4 wt % sodium salicylate in 0.32 M NaOH)50 μL (1 wt % cat.)11:0.2(30)

All of the reagents are added into the analyte consecutively as mentioned below.

All of the reagents are added into the analyte consecutively as mentioned below. The maximum absorbance value (Aλmax) obtained from the UV–vis spectrum corresponds to the ammonia concentration present in the analyte. The analytes used in this work are prepared in Milli-Q water, which inherently contains a certain amount of ammonia. Therefore, to remove the background ammonia contribution (Milli-Q water and indophenol reagent chemicals) from the analyte, we subtracted the Aλmax of the blank from the analyte’s value (denoted ΔAbsorbance).The indophenol method and procedures P1 (with citrate) and P3 (without citrate) were selected to quantify ammonia in a 0.2 ppm ammonia solution (using NH4Cl) containing 0.1 mM metal ions (Ce3+, Cr3+, Ni2+, Fe3+). The 0.1 mM metal ion solutions were prepared using Ce(NO3)3·6H2O, CrCl3·6H2O, Ni(NO3)2·6H2O, and Fe(NO3)3·9H2O. Herein, the blank solution contains Milli-Q water with a 0.1 mM metal ion. The calibration curve was obtained using procedure P1 with different concentrations of an ammonia standard (prepared with NH4Cl), with NH4+ concentrations varying from 0 to 1 ppm in 0.05 M H2SO4 and 0.1 M Na2SO4 separately. The absorbance values (at λmax = 645 nm) of the ammonia standards are incorporated in the calibration curve after subtracting the contribution of the blank from each of them as given in eq . Ammonia solution for the containment test, in Figure S10, was prepared by serial dilution of a commercial 25% ammonia solution (NH4OH) using a 0.1 M Na2SO4 aqueous solution. The final concentration of ammonia obtained after serial dilution was calculated from the calibration plot (Figure S5b) to be 0.3 ppm.

Quantification of NO2– and NO3– by the Griess Method[28]

The Griess method is used for the determination of NO2– and NO3– ions’ concentration in the electrolyte. The diazotizing reagent was obtained by adding 1 mL of concentrated HCl (37%) and 0.1 g of sulfadiazine (SULF) in a volumetric flask, which was filled up to 10 mL with water. The coupling reagent was prepared by dissolving 0.01 g of N-(1-napthyl)ethylenediamine dihydrochloride (NED) in 10 mL of H2O. All of the Griess reagents were stored in a refrigerator (4 °C) for further use. For the detection of NO2– ion quantity, first 0.50 mL of 0.1 M HCl was added to 0.5 mL of a sample. Further, 25 μL of SULF and 25 μL of NED were added sequentially, resulting in a pink coloration of the solution upon incubating for 20 min at ambient temperature. The UV–vis measurement was taken immediately. For quantification of NO3– ions, a similar protocol was used like for the NO2– ion with the addition of extra 50 μL of a 0.02 wt % vanadium(III) chloride solution (prepared in 6 M HCl) at the end. Further, the mixture was incubated at 60 °C in a water bath for 25 min and cooled to room temperature before the UV–vis measurement.

Electrochemical Measurements

All of the electrochemical measurements were carried out in an airtight two-chamber glass H-cell separated by a Nafion 117 membrane (Figures S6 and S7). A three-electrode system was used with an electrocatalyst on conducting Ni foam, an aqueous Ag/AgCl (1 M KCl) electrode (CHI 111), and a platinum wire (CHI Instruments Inc.) as the working, reference, and counter electrodes, respectively. Prior to the electrochemical experiment, N2/Ar was purged in the electrolyte (0.1 M Na2SO4) of the cathode chamber at 20 mL/min for 30 min. During the electrochemical reaction, the catholyte (electrolyte in the cathode chamber) was continuously purged with N2/Ar gas with the same flow rate of 20 mL/min. Linear sweep voltammetry (LSV) and chronoamperometry (CA) were performed with a potentiostat (Biologic Science Instruments, Inc., 760E). The applied potential measured against the Ag/AgCl (1 M KCl) reference electrode was converted to a reversible hydrogen electrode (RHE) after calibrating it in 0.1 M Na2SO4 electrolyte. Electrolysis of the catalyst in the Ar medium was performed first, and after performing chronoamperometry in the Ar medium, the same working electrode was used for electrolysis in the nitrogen medium. The initial volume of the electrolyte in both cathode and anode chambers was 23 mL. A total of 1.9 mL of aliquots for ammonia detection were collected from the purged electrolyte (30 min of purging) of the cathode, the anode chamber, and the trap prior to electrochemical measurements, and the same after the electrochemical process. To 1.9 mL of electrolyte, 100 μL of 2 M H2SO4 was added to stabilize the soluble ammonia (volatility of ammonia increases with pH), and it was stored in a refrigerator at 4 °C. The cathode and anode chambers were continuously agitated with a Teflon-lined magnetic stirrer at 500 rpm during all of the electrochemical measurements. Then, a 12 mL solution of 0.05 M H2SO4 was put as a trap to contain the ammonia at the outlet of the cathode chamber. The ammonia estimation by the indophenol method (procedure P1) was done for each set of electrochemical reaction within 4 h to avoid ammonia contamination upon storage. For all of the purposes in this work, fresh Milli-Q water with less than 12 h of storage time was used (to avoid increase in ammonia contamination upon storage).

Calibration of Reference Electrodes and Conversion to RHE

The calibration Ag/AgCl (1 M KCl) reference electrode was performed in a standard three-electrode system. A polished and activated Pt wire (CHI Instruments Inc.) was used as the working electrode, and a high-surface-area Pt coil (CHI Instruments Inc.) was used as the counter electrode. The Ag/AgCl (1 M KCl) electrode was used as the reference electrode. The electrolyte (0.1 M Na2SO4) was prepurged and saturated with high-purity H2 (VICI DBS hydrogen generator, 99.999% purity) for 1 h prior to the experiments. Cyclic voltammetry (CV) was then run at a scan rate of 1 mV s–1 with continuous H2 bubbling near the working electrode (Pt wire) (Figure S9). The potential at which the current crossed zero is taken to be the thermodynamic potential for the hydrogen electrode reactions. In this case, the average potential of the two lines crossing zero current (hydrogen oxidation and hydrogen reduction) was calculated. In 0.1 M Na2SO4, the zero current point is at −0.521 V, so E (RHE) = E (Ag/AgCl) + 0.521 V.

Results and Discussion

Pitfalls in Ammonia Quantification by the Indophenol Method

The indophenol method generally uses a coloring agent (phenol/salicylic acid), an oxidant (NaClO), and a catalyst (nitroprusside) to detect ammonia in the form of indophenol, as described in Figure S1.(23) In the literature, there are four sets of procedures commonly used to estimate the ammonia produced in ENR, which differed from one another with respect to the mole ratio of salicylate to NaClO employed, the order of addition of reagents, and the use of sodium citrate.[16,26,29,30] To understand the influence of these factors further, we have selected all four indophenol procedures for quantification analysis (Table ). To start with, we estimated the ammonia inherently present in Milli-Q water by these procedures, and the UV–vis absorption results are shown in Figure a. Among all of the procedures employed, only one (procedure P1) showed a distinct absorption maximum at 645 nm, which was stable for more than 2 h (Figures a and S2). Next, a known amount of ammonium chloride was added to the Milli-Q water (equivalent to 0.3 ppm of ammonia solution) and the quantification was repeated for all four procedures. Among the four procedures, procedure P2 (with a high NaClO/salicylate mole ratio, 14:1) failed to show any UV–vis absorption maxima (λmax) (Figure b). The absence of color for procedure P2 in the inset (Figure b) further confirms the invalidity of this procedure to estimate ammonia at lower concentrations. In the other three procedures, a concomitant increase in the absorbance value with respect to blank Milli-Q water was observed at their λmax. Furthermore, the relevance of citrate addition (scavenger of interfering metal ions in the indophenol method[31]) is exemplified in quantifying 0.2 ppm ammonia standard in the presence of Ce3+, Cr3+, Fe3+, and Ni2+ metal ions (experimental details are provided in the experimental section, Section ) using the procedures P1 (with citrate) and P3 (without citrate). The experimental data (Figures c,d and S3) show only ±4% variation in absorbance maxima for all of the cation-containing standards analyzed by procedure P1, whereas a large variation in absorbance maxima, +40% (Fe3+) to −11% (Cr3+), was observed for procedure P3. Thus, based on the above control experiments, we have adopted the robust indophenol procedure P1 in our quantification studies to avoid any false results associated with these metal ions.
Figure 2

Optimization of the indophenol method for ammonia quantification. UV–visible absorption spectra of (a) Milli-Q water and (b) Milli-Q water containing 0.3 ppm ammonia (prepared using NH4Cl) were analyzed with four different indophenol procedures used in the literature as tabulated in Table . The inset provides the optical image of the analyte after incubating with indophenol reagents according to the adopted procedure. The presence of metal ions (0.1 mM) in the 0.2 ppm ammonia standard showed a variation in the increase of the absorbance value (ΔA) with respect to the blank at λmax by (c) ±4% for procedure P1 in which sodium citrate was used and (d) +40% (Fe3+) and −11% (Cr3+) for procedure P3 in which no citrate was used. (e) Successive UV–vis scan of indophenol-stained Milli-Q water, following procedure P1 (the inset shows the maximum variation of 0.007 in the absorbance value at λmax = 645 nm). (f) Change in the absorbance value (ΔA) for ammonia calibration standards (0.01, 0.03, and 0.05 ppm) with respect to the blank (Milli-Q water). The horizontal dotted line lies at ΔA = 0.007, below which the concentration of ammonia cannot be estimated accurately.

Optimization of the indophenol method for ammonia quantification. UV–visible absorption spectra of (a) Milli-Q water and (b) Milli-Q water containing 0.3 ppm ammonia (prepared using NH4Cl) were analyzed with four different indophenol procedures used in the literature as tabulated in Table . The inset provides the optical image of the analyte after incubating with indophenol reagents according to the adopted procedure. The presence of metal ions (0.1 mM) in the 0.2 ppm ammonia standard showed a variation in the increase of the absorbance value (ΔA) with respect to the blank at λmax by (c) ±4% for procedure P1 in which sodium citrate was used and (d) +40% (Fe3+) and −11% (Cr3+) for procedure P3 in which no citrate was used. (e) Successive UV–vis scan of indophenol-stained Milli-Q water, following procedure P1 (the inset shows the maximum variation of 0.007 in the absorbance value at λmax = 645 nm). (f) Change in the absorbance value (ΔA) for ammonia calibration standards (0.01, 0.03, and 0.05 ppm) with respect to the blank (Milli-Q water). The horizontal dotted line lies at ΔA = 0.007, below which the concentration of ammonia cannot be estimated accurately. The presence of a trace amount of ammonia from the surrounding and possibly from indophenol reagents[14,16] (inherent) results in variable absorbance maxima for blank Milli-Q water, which cannot be nullified (Figure S4a). To avoid such fluctuations cropping up in the measurement of ammonia concentration, we have used the difference in the absorbance value (ΔA at 645 nm) obtained for the electrolyte before and after ENR, rather than their actual absorbance values (according to eq , experimental Section ). The ΔA value (at 645 nm) obtained for the addition of a known amount of ammonium chloride in the electrolyte was used for the calibration curve (Figure S5) in our method. It is to be noted that the ΔA value below 0.007 does not have any significance as successive UV–visible scans (without repositioning or refilling the cuvette) of Milli-Q water stained with indophenol reagents themselves show a variation of ΔA = 0.007 (at 645 nm, Figure e). Such a variation in the ΔA value for successive UV–vis scans was observed even for the 0.3 ppm ammonia standard (Figure S4b), suggesting it to be the inherent instrument precision limit (0.007).[32] It is to be noted that in other labs the observed inherent instrument precision may differ from 0.007 and may also vary with absorbance. In our case, the observations disregard the ΔA value below 0.007 obtained for any analyte. It is important to note that the calibration standards prepared with ammonia concentration below 0.05 ppm have absorbance values (ΔA) less than the instrument precision value, i.e., 0.007 (Figure f). Here, we realize the limitation in accurately estimating the ammonia concentration below 0.05 ppm in an aqueous medium and set it as the lower limit of quantitation (LOQ) for the ammonia concentration (precise calculation for LOQ along with the limit of detection (LOD) is provided in the Supporting Information). In other words, ammonia concentration below 0.05 ppm was not considered as a positive result for ENR.

Electrochemical Nitrogen Reduction Studies

Based on the above experimental findings, we have proposed a stepwise protocol for performing ENR (Scheme ) and have revisited the ENR activity of two recently reported electrocatalysts, Au3Pd alloy and zinc sulfide on nickel foam (NF)[26,27] with our optimized electrochemical setup (see the Supporting Information for details, Figures S6–S8 and S10).
Scheme 1

Protocol for Performing ENR

The stepwise procedure highlights the necessity of choosing the appropriate indophenol method along with establishment of the LOQ (lowest limit of quantitation) prior to electrochemical ENR analysis. In addition to it, emphasis is also given toward performing prolonged electrochemical reduction in Ar at the chosen potential until no ammonia is detected in the electrolyte (the loop is marked with red-colored arrows in the scheme) before performing electroreduction of N2. This will take care of the reducible N species or NH3 inherently present in the catalyst material, which are not removed by the conventional precatalysis treatment (exemplified below with the case study of ZnS/NF). The details of each step are provided in the Supporting Information.

Until stabilized polarization curves (LSV) are obtained.

Check the ENR activity at other potentials starting from step 4.

Protocol for Performing ENR

The stepwise procedure highlights the necessity of choosing the appropriate indophenol method along with establishment of the LOQ (lowest limit of quantitation) prior to electrochemical ENR analysis. In addition to it, emphasis is also given toward performing prolonged electrochemical reduction in Ar at the chosen potential until no ammonia is detected in the electrolyte (the loop is marked with red-colored arrows in the scheme) before performing electroreduction of N2. This will take care of the reducible N species or NH3 inherently present in the catalyst material, which are not removed by the conventional precatalysis treatment (exemplified below with the case study of ZnS/NF). The details of each step are provided in the Supporting Information. Until stabilized polarization curves (LSV) are obtained. Check the ENR activity at other potentials starting from step 4. The Au3Pd/NF electrocatalyst,[26] synthesized by a simple galvanic replacement reaction as reported in the literature, was characterized using XRD and FESEM imaging (Figure S11). The absence of NO and ammonia contamination from Au3Pd/NF was confirmed by carrying out electrochemical reduction in argon (Figure S12). Estimation of ammonia in the catholyte showed more or less the same absorbance maxima (at λmax = 645 nm) as the one obtained before electrolysis (Figure S13a). Quantitation of ammonia after carrying out the electrochemical nitrogen reduction (chronoamperometry performed at −0.1 V vs RHE in 0.1 M Na2SO4) showed no significant change in the absorbance maxima (ΔA < 0.007) as compared to the reaction carried out in an argon flow (Figure S13b with a detailed analysis provided in Table S2). As the concentration of ammonia measured after the ENR is lower than the LOQ (<0.05 ppm), we considered this as an inactive catalyst for electrochemical nitrogen reduction to ammonia (Figure a). In contrast, the report claimed the ammonia production rate to be 7.85 μg h–1 mgcat–1 (for Au3Pd/NF synthesized using the Pluronic F-127 surfactant).[26] Interestingly, the concentration of ammonia in the electrolyte calculated from its calibration curve is below 0.05 ppm although the derived production rate is huge (Figure a).
Figure 3

Revisiting the ENR activity of the electrocatalyst. The ammonia concentrations generated in the catholyte and trap after electrochemical reduction in nitrogen (N2) and argon (Ar) gas using (a) Au3Pd/NF at −0.1 V vs RHE and (b) ZnS/NF at −0.5 V vs RHE are presented along with their reported data, denoted “Lit.” The ammonia yield, which is calculated from the ammonia concentration, is also provided in the graphs. It must be noted that according to our protocol (Scheme ), the ammonia concentration generated below 0.05 ppm post electrolysis is considered insignificant. In our work, Au3Pd/NF produced 0.03 ppm (inconsiderable) ammonia concentration post electrolysis in both Ar and N2 atmospheres. In the case of ZnS/NF, the concentration of ammonia generated after electrolysis in the argon atmosphere was >0.05 ppm until four consecutive cycles, after which an insignificant amount of ammonia was produced in both Ar and N2 atmospheres. It must be noted that the ammonia production rate in the case of ZnS/NF was reported as 5.27 × 10–10 mol s–1 cm–2, which is equal to 32.2 μg h–1 cm–2.

Revisiting the ENR activity of the electrocatalyst. The ammonia concentrations generated in the catholyte and trap after electrochemical reduction in nitrogen (N2) and argon (Ar) gas using (a) Au3Pd/NF at −0.1 V vs RHE and (b) ZnS/NF at −0.5 V vs RHE are presented along with their reported data, denoted “Lit.” The ammonia yield, which is calculated from the ammonia concentration, is also provided in the graphs. It must be noted that according to our protocol (Scheme ), the ammonia concentration generated below 0.05 ppm post electrolysis is considered insignificant. In our work, Au3Pd/NF produced 0.03 ppm (inconsiderable) ammonia concentration post electrolysis in both Ar and N2 atmospheres. In the case of ZnS/NF, the concentration of ammonia generated after electrolysis in the argon atmosphere was >0.05 ppm until four consecutive cycles, after which an insignificant amount of ammonia was produced in both Ar and N2 atmospheres. It must be noted that the ammonia production rate in the case of ZnS/NF was reported as 5.27 × 10–10 mol s–1 cm–2, which is equal to 32.2 μg h–1 cm–2. The unusually high production rate in spite of the low concentration of ammonia is due to the amplification factor arising from the volume of the electrolyte and the amount of catalyst used (details are provided in the Supporting Information). The ZnS nanostructure grown on the nickel foam (ZnS/NF)[27] is another electrocatalyst we have tested for ENR activity (Figure S14). Since the synthesis of ZnS/NF involved the nitrogen-based precursor (thiourea), it was subjected to an acid wash to remove any occluded ammonia produced during synthesis (Figure S15). The acid-washed ZnS/NF electrocatalyst was first tested in an argon environment (20 mL/min flow) while applying a constant potential of −0.5 V vs RHE (as reported in the literature) for 2 h (Figure S16b). The catholyte after the reaction was analyzed by the indophenol method, which showed ammonia concentration above 1 ppm. However, with subsequent runs, the production rate of ammonia decreases gradually and goes below 1 μg h–1 cm–2 (below 0.05 ppm, ΔA ∼ 0.007) in the 5th cycle (Figures b and S17). Further electrochemical reduction performed under nitrogen with the same electrode (after the catalyst was subjected to 5 cycles under argon) did not produce any ammonia (below 0.05 ppm), which is in sharp contrast to the ammonia production rate of 32.2 μg h–1 cm–2 reported in the literature (see Figure b and Table S3 for more information).

Conclusions

In conclusion, through some definitive control experiments, we have standardized the protocol to quantify ammonia in an aqueous electrolyte at a very low concentration in the ENR reaction using the indophenol method. Our observation suggests that the choice of a proper indophenol procedure (with an appropriate salicylate/NaClO ratio, inclusion of citrate) is a decisive factor in accurately determining the concentration of ammonia at sub-ppm levels. It is also evident from our investigations that the quantitation of ammonia by the indophenol method below a 0.05 ppm (LOQ) concentration in the catholyte falls in the range of experimental errors and converting this concentration into production rate will be misleading and has to be avoided. The protocol we have established would help researchers screen the catalysts in the first place before proceeding to costlier 15N2 tests for further confirmation. Since the ammonia produced from ENR is exceedingly low, we suggest that the performance metric of an electrocatalyst needs to be mentioned in terms of concentration of ammonia along with the normalized production rate. It is because the ammonia concentration is the direct quantity we measure using the UV–vis spectrometric method (particularly by indophenol method) and it has limitations in measuring at very low concentrations. In addition, we suggest that researchers in this field always provide the obtained UV–vis spectra (with the absorbance value) and also document the electrolyte volume and the amount of catalyst loaded for the ENR process to remove any ambiguity when others try to reproduce the performance of a reported catalyst. As this field is in its infancy stage and many state-of-the-art protocols to ascertain the production of ammonia are still emerging, it is imperative to provide all minute experimental details along with every possible pitfall we encounter in this analysis to assess the performance of a catalyst devoid of false positives.
  10 in total

1.  Electrochemical nitrogen reduction to ammonia at ambient conditions on nitrogen and phosphorus co-doped porous carbon.

Authors:  Pengfei Song; Hao Wang; Li Kang; Baocheng Ran; Honghong Song; Rongmin Wang
Journal:  Chem Commun (Camb)       Date:  2018-12-19       Impact factor: 6.222

2.  A rigorous electrochemical ammonia synthesis protocol with quantitative isotope measurements.

Authors:  Suzanne Z Andersen; Viktor Čolić; Sungeun Yang; Jay A Schwalbe; Adam C Nielander; Joshua M McEnaney; Kasper Enemark-Rasmussen; Jon G Baker; Aayush R Singh; Brian A Rohr; Michael J Statt; Sarah J Blair; Stefano Mezzavilla; Jakob Kibsgaard; Peter C K Vesborg; Matteo Cargnello; Stacey F Bent; Thomas F Jaramillo; Ifan E L Stephens; Jens K Nørskov; Ib Chorkendorff
Journal:  Nature       Date:  2019-05-22       Impact factor: 49.962

3.  Energy-Efficient Nitrogen Reduction to Ammonia at Low Overpotential in Aqueous Electrolyte under Ambient Conditions.

Authors:  Dabin Wang; Luis Miguel Azofra; Moussab Harb; Luigi Cavallo; Xinyi Zhang; Bryan H R Suryanto; Douglas R MacFarlane
Journal:  ChemSusChem       Date:  2018-09-04       Impact factor: 8.928

4.  Achieving a Record-High Yield Rate of 120.9 μgNH3  mgcat.-1  h-1 for N2 Electrochemical Reduction over Ru Single-Atom Catalysts.

Authors:  Zhigang Geng; Yan Liu; Xiangdong Kong; Pai Li; Kan Li; Zhongyu Liu; Junjie Du; Miao Shu; Rui Si; Jie Zeng
Journal:  Adv Mater       Date:  2018-08-10       Impact factor: 30.849

5.  Ambient N2 fixation to NH3 electrocatalyzed by a spinel Fe3O4 nanorod.

Authors:  Qin Liu; Xiaoxue Zhang; Bing Zhang; Yonglan Luo; Guanwei Cui; Fengyu Xie; Xuping Sun
Journal:  Nanoscale       Date:  2018-08-02       Impact factor: 7.790

6.  Metal-Sulfur Linkages Achieved by Organic Tethering of Ruthenium Nanocrystals for Enhanced Electrochemical Nitrogen Reduction.

Authors:  Muhammad Ibrar Ahmed; Chuangwei Liu; Yong Zhao; Wenhao Ren; Xianjue Chen; Sheng Chen; Chuan Zhao
Journal:  Angew Chem Int Ed Engl       Date:  2020-09-15       Impact factor: 15.336

7.  Boron and nitrogen dual-doped carbon nanospheres for efficient electrochemical reduction of N2 to NH3.

Authors:  Shenglin Xiao; Fang Luo; Hao Hu; Zehui Yang
Journal:  Chem Commun (Camb)       Date:  2019-12-11       Impact factor: 6.222

8.  Mesoporous Au3Pd Film on Ni Foam: A Self-Supported Electrocatalyst for Efficient Synthesis of Ammonia.

Authors:  Hongjie Yu; Ziqiang Wang; Shuli Yin; Chunjie Li; You Xu; Xiaonian Li; Liang Wang; Hongjing Wang
Journal:  ACS Appl Mater Interfaces       Date:  2019-12-23       Impact factor: 9.229

Review 9.  Ammonia Detection Methods in Photocatalytic and Electrocatalytic Experiments: How to Improve the Reliability of NH3 Production Rates?

Authors:  Yunxuan Zhao; Run Shi; Xuanang Bian; Chao Zhou; Yufei Zhao; Shuai Zhang; Fan Wu; Geoffrey I N Waterhouse; Li-Zhu Wu; Chen-Ho Tung; Tierui Zhang
Journal:  Adv Sci (Weinh)       Date:  2019-02-15       Impact factor: 16.806

  10 in total

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