Electrochemical Characterization of Electrodeposited Copper Catalyst for CCU

1. Introduction

Mitigating climate change necessitates urgent action to reduce CO₂ emissions. Achieving net zero CO₂ emissions by 2050 is critical to limit the temperature rise to below 1.5 °C, in line with the Paris Agreement (COP21) objectives [1]. To address this challenge, the development of CO₂ capture technologies is a priority. Currently, the most advanced industrial technology employs aqueous amine solutions such as monoethanolamine (MEA), methyldiethanolamine (MDEA) and 2-amino-2-methylpropanol (AMP) for CO₂ capture. This process entails direct CO₂ capture from flue gas stream and its subsequent release by heating the CO₂-rich amine capture media in a desorber unit at approximately 120°C [2]. The regenerated amine then re-enters the capture cycle. However, the regeneration step, accounting for up to 30% of the total plant energy output, is highly energy-intensive [3]. This issue may be overcome by regenerating the CO₂-rich amine media using electrochemical CO₂ reduction (ECR) instead. This approach features the direct transformation of amine-CO₂ adducts, such as carbamates, into valuable chemicals [4]. The seamless integration of amine-based CO₂ capture and ECR demonstrates good synergy. This approach not only bypasses challenges related to CO₂ transportation and storage but also eradicates the necessity for regenerating capture media through the thermal release of molecular CO₂ [5].

ECR is an emerging field, evolving independently from carbon capture technologies. It presents significant synergies with other climate change challenges, notably in storing surplus renewable electricity. ECR converts excess electricity into valuable, energy-dense products like CO, ethylene, ethanol etc. The output product spectrum depends on the applied potential, catalyst, and cell configuration [6]. Copper is unique in promoting valuable C₂+ products like ethylene and is therefore widely employed as a catalyst [7]. Achieving economic viability in ECR hinges on meeting specific performance benchmarks, including current density, Faradaic efficiency (FE), energy efficiency (EE), and stability [8]. Recent research has made significant strides in improving current density, FE, and EE. Notably, current densities over 1 A cm^-2 with 45% EE for ethylene production using copper gas diffusion electrodes (GDEs) have been achieved [9]. Ongoing efforts aim to enhance selectivity toward C₂+ products through advanced copper-based catalysts [10,11,12]. However, stability improvements remain a less explored yet critical aspect for viable ECR. Copper catalysts often undergo rapid degradation due to surface reconstruction, poisoning, and carbonate salt precipitation [13]. Studies by Huang et al. [14] and Simon et al. [15] show that cathodic potential drives copper catalyst surface reconstruction and refaceting. This process results in decreased selectivity towards C₂+ products, undermining long-term catalyst performance [16,17,18,19]. Another challenge for stable ECR is carbonate salt precipitation on the catalyst surface [20,21,22]. The local high pH near the electrode, due to HO^- production in the CO₂ reduction reaction, facilitates carbonate salt formation through reaction with cations.

Recent advancements in electrochemical CO₂ reduction (ECR) have highlighted pulse ECR as a method to enhance long-term process performance [23]. Pulse ECR involves interspersing short anodic segments with longer cathodic ones to regenerate the catalytic properties of copper by inducing oxidation. Obasanjo et al. [24] demonstrated that this oxidation process reactivates C₂+ active sites by removing Cu-OH, which gradually deactivates the catalyst. Xu et al. [21] successfully employed pulse ECR to sustain high Faradaic efficiency (FE) towards C2+ products over 36 hours, observing that Cu(I) oxide formation is advantageous for C2+ product formation and can be regenerated through anodic pulsing. Similarly, Zhang et al. [25] found that a combination of Cu(0) and Cu(I) states favours C₂+ products, maintaining a high FE (70%) towards ethylene across 145 hours of operation using pulse ECR. Complementary studies have shown that appropriate pulse strategies can enhance and modulate long-term selectivity of ECR [26,27], while also mitigating catalyst poisoning [28] and carbamate salt formation [21,29].

Research on ECR, including pulse ECR has largely focused on using aqueous carbonate (KOH + CO₂) or bicarbonate (KHCO₃ + CO₂) solutions. Increasing efforts are now directed towards integrating ECR with amine-based CO₂ capture. Various studies have reported carbamate reduction to CO [30], formate [31,32], or both [33] using metal electrodes like copper [30,32]. However, the long-term stability of these catalytic properties remains unexplored. Additionally, the impact of amines on copper corrosion is a growing concern [5], with some studies suggesting significant copper degradation in MEA under halted cathodic potential [34], which necessitates further investigation.

In this study, we explore the electrochemical and corrosion properties of electrodeposited copper in amine-based electrolytes under CO₂-lean and -rich conditions. We also examine the stability of the copper catalyst under cathodic polarization relevant to CO₂ reduction. Different pulse polarization strategies are tested to assess the impact of pulse ECR in amine media.

2. Materials and Methods

2.1. Specimen Preparation and Characterisation

Copper was electrodeposited onto a copper substrate using a method detailed in the Supplementary Information. Following electrodeposition, specimens were selectively masked with resin provided by Belzona Ltd. (UK, reference 1395) resin, resulting in an exposed surface area of approximately 1 cm² for each specimen. To characterize the surfaces of these specimens, an optical microscope BX41M-LED from Olympus (JPN) and a Sigma 1455EP scanning electron microscope (SEM) from Ziess (GER) were employed.

2.2. Amine Media

Four amine-based media, commonly employed for CO₂ capture, were evaluated:

• 30 wt.% Monoethanolamine (MEA), CAS: 141-43-5, a primary amine extensively utilized for CO₂ capture [2].
• 37 wt.% Methyldiethanolamine (MDEA) CAS: 105-59-9, a tertiary amine
• 30 wt.% MDEA + 21 wt.% piperazine (PZ), CAS: 110-85-0, generally used to improve capture kinetics [35].
• 30 wt.% 2-Amino-2-methyl-1-propanol (AMP), CAS: 124-68-5, a sterically hindered primary amine known for its elevated CO₂ absorption capacity [36].

The anolyte for these experiments was 0.5 M potassium chloride (KCl) solution. Additionally, 0.5 M KCl was incorporated into the amine solutions to enhance their electrical conductivity. All chemicals used in solution preparation were of laboratory grade and supplied by Merck Life Science UK Ltd. (UK).

In subsequent discussions and analyses, these solutions are referred to as MEA, MDEA, MDEA/PZ, and AMP for simplicity.

2.2. Electrochemical Tests

Electrochemical experiments were conducted using a Biologic (FR) VMP-300 potentiostat and a 100 mL H-cell sourced from Dek research (US). The experimental setup featured anodic and cathodic compartments, separated by a Nafion 117 proton exchange membrane (Dupont, US) which underwent appropriate activation before use. The reference electrode comprised an Ag/AgCl in 3.5 M KCl, positioned in a Luggin capillary filled with 3.5 M KCl to isolate it from the amine electrolyte. The capillary's tip was situated 5 mm from the specimen. A platinum mesh served as the counter electrode. The cell design included gas inlet/outlet provisions for purging the solution with CO₂. Each specimen was kept at -0.5 V relative to the Open Circuit Potential (OCP) for 5 minutes before testing to remove the air-formed oxide layer.

Linear polarization resistance (LPR), potentiodynamic polarization (PDP), and cyclic voltammetry (CV) tests were performed after recording and stabilizing the OCP for 1 h. To ensure reproducibility, each measurement was conducted in triplicate. For brevity, Figure 2 displays a single representative polarization scheme per experimental condition, with the full dataset accessible in Figure 1 of the Supplementary Information document. LPR results are presented in Supplementary Information Figure 2. The test solutions were maintained at ambient laboratory conditions (20 ± 2 °C) and could be CO₂-purged as required. LPR tests utilized a potential offset of ±20 mV relative to OCP at a scan rate of 0.125 mV s^-1. PDP involved potential sweeping from -0.2 V to +0.2 V versus OCP at a rate of 10 mV min^-1. CV scans were conducted at 20 mV s^-1 scan rate, reversing the scan when the current density reached |10| mA cm^-2 for both cathodic and anodic polarizations.

Figure 1. Three modes of chronopotentiometry: (1) continuous polarization at -10 mA cm^-2 for 60 h; (2) pulse mode 1, 45 min at -10 mA cm^-2 for 24 s at +1 mA cm^-2 repeated 80 times; (3) pulse mode 2, 50 s at -10 mA cm^-2 for 2 s at +1 mA cm^-2 repeated 4320 times.

Figure 1. Three modes of chronopotentiometry: (1) continuous polarization at -10 mA cm^-2 for 60 h; (2) pulse mode 1, 45 min at -10 mA cm^-2 for 24 s at +1 mA cm^-2 repeated 80 times; (3) pulse mode 2, 50 s at -10 mA cm^-2 for 2 s at +1 mA cm^-2 repeated 4320 times.

Figure 2. Potentiodynamic polarization of copper specimens in the different amine-based capture media. (a) without CO₂ and (b) with CO₂ purging. Scan rate 10 mV min^-1.

Figure 2. Potentiodynamic polarization of copper specimens in the different amine-based capture media. (a) without CO₂ and (b) with CO₂ purging. Scan rate 10 mV min^-1.

Chronopotentiometry experiments were designed to simulate 60 hours of ECR. Three strategies, that included alternating anodic and cathodic segments, were implemented as detailed in Figure 1. Anodic segments were conducted at +1 mA cm^-2, while cathodic segments operated at -10 mA cm^-2, cumulatively totalling 60 hours for cathodic segments. Pulse mode 1 consisted of a 24-second anodic segment every 45 minutes, and pulse mode 2 involved a 2-second anodic segment every 50 seconds.

Electrochemical tests underwent iR compensation utilizing the potentiostat's built-in feature, which is based on high-frequency impedance measurements. The average cell resistances determined for each media are systematically tabulated in Supplementary Information Table S1.

3. Results

3.1. Electrochemical Characterisation of Electrodeposited Copper in Amine Media

Potentiodynamic polarizations were performed in triplicate under both CO₂-free and CO₂-purged conditions across various amine media. For each scenario, a representative curve was selected for display in Figure 2, with the comprehensive set of polarization data provided in the Supplementary Information Figure 1. The Tafel extrapolation method was employed to estimate the corrosion current density (j_corr) [37]. The average j_corr values, together with the corresponding corrosion potentials (E_corr), are compiled in Table 1.

In environments devoid of CO₂, j_corr values for all amines were lower compared to 0.5 M KCl. Specifically, MDEA and MDEA/PZ exhibited reduced j_corr values relative to MEA and AMP, with the latter two showing j_corr values comparable to KCl. Upon introducing CO₂, a notable shift in E_corr towards more anodic potentials occurred for all amines, attributable to the dissolution of CO₂ and the formation of carbonate/bicarbonate species. Concurrently, the introduction of CO₂ resulted in an increase in j_corr across all amines. The relative order of j_corr values remained consistent with the CO₂-free cases: MEA and AMP exhibited higher j_corr, exceeding that of KCl, while MDEA and MDEA/PZ maintained significantly lower values. Polarization resistances (R_p) data, derived from LPR measurements, were consistent with j_corr. Lower R_p values, indicative of higher corrosion rates, were observed for CO₂-loaded MEA and AMP, whereas CO₂-free MDEA and MDEA/PZ demonstrated higher resistances.

CV scans, presented in Figure 3, reveal distinct electrochemical behaviours of copper in various amine media. For comparative purposes, CV experiments were also conducted in 0.5 M KCl. In CO₂-lean amine media, two oxidation peaks (A and B) were identified and two reduction peaks (C and D). It is well established that copper oxidizes to form either Cu(I) or Cu(II) [38]. During the anodic sweep, the initial peak (A) is attributed to the formation of Cu(I), while the subsequent peak (B) corresponds to Cu(II) oxidation, both manifesting as copper oxides/hydroxides and their hydrated forms. The oxidation current increase beyond peak B signifies the formation of soluble copper ions such as CuO₂^-, until the onset of oxygen evolution at more anodic potentials. The onset potential for peak A remains relatively consistent across all CO₂-free amine media, approximately at 0.45 V. However, the onset for peak B varies significantly, indicating a more complex oxidation mechanism, in line with previous findings in KOH solutions [39]. In MEA, the lowest onset potential leads to the overlapping of peaks A and B. In contrast, MDEA, MDEA/PZ, and AMP exhibit distinct B peaks at more anodic potentials, at -0.27 V, -0.15 V, and -0.27 V respectively. Peaks C and D are associated with the reduction of Cu(I) and Cu(II) species, while the highest cathodic current surge is attributed to the hydrogen evolution reaction (HER).

In CO₂-rich amine media, only two peaks, labelled A_CO2 and B_CO2, are evident. Peak A_CO2 could represent the overlap of peaks A and B, indicating the concurrent formation of both Cu(I) and Cu(II) species, or it might signify the exclusive formation of Cu(II) species. The former scenario seems more probable, as the overlapping of peaks A and B has been previously reported in high pH conditions [39], likely influenced by CO₂ purging. The onset oxidation potentials in various amines are closer in the CO₂-rich environment, recorded at -0.21 V, -0.27 V, -0.17 V, and -0.25 V for MEA, MDEA, MDEA-PZ, and AMP, respectively. This observation underscores the significant impact of the presence of CO₂ on copper oxidation and supports previous PDP and LPR data. Copper oxidizes more readily in CO₂-rich media, as evidenced by a steeper increase in oxidation current at more cathodic potentials, except for MEA, which exhibits a slightly higher oxidation onset potential in CO₂-rich conditions. In CO₂-rich amines, the most anodic current is either due to HER or the CO₂ reduction reaction (CO₂RR),and is shifted towards more anodic potentials. This shift suggests that CO₂RR may have a more anodic onset potential than HER, leading to an observable increase in current density on the CV scan for CO₂-purged media.

3.1. Chronopotentiometry

Specimens underwent cathodic polarization for a cumulative duration of 60 hours, employing varied pulse strategies. These strategies encompassed continuous cathodic polarization, pulse mode 1, and pulse mode 2, detailed in Figure 1. The potential as a function of time was closely monitored, with the corresponding cathodic chronopotentiometry results displayed in Figure 4. Anodic chronopotentiometry results are similarly detailed in Figure 5.

Chronopotentiometry results for continuous cathodic polarization over 60 hours in MEA, MDEA, and AMP are illustrated in Figure 4a. In MDEA/PZ, this experiment was hindered by the formation of carbonate salts, which obstructed the CO₂ gas inlet after only 2-3 hours. Similar carbonate salt precipitation was observed in MDEA, leading to an unstable cathodic potential that progressively shifted towards more cathodic values, as depicted in Figure 4a. In contrast, the potentials in AMP demonstrated greater stability, albeit with a slight decrease over time. Notably, MEA exhibited the most stable potential, concluding the experiment at a potential 20 mV higher than the initial value.

The influence of pulse strategies on potential evolution for the various amine solutions is highlighted in Figure 4b–d. Employing a lower frequency pulse strategy (pulse mode 1) consistently improved potential stability across all amine solutions. In the case of MDEA, this strategy resulted in a stable potential decrease beyond 55 hours, contrasting with the trend observed under continuous polarization. For MEA and AMP, pulse mode 1 induced a gradual electropositive shift in potential, reaching increments of +70 mV and +65 mV from their initial values, respectively. The adoption of a higher frequency of anodic segments (pulse mode 2) demonstrated diverse outcomes. In MEA, pulse mode 2 more significantly improved potential stability compared to pulse mode 1, achieving an increase of +125 mV compared to the initial value. In contrast, for AMP, the potential under pulse mode 2 initially remained stable but began to decline after 45 hours, aligning more closely with the behaviour observed under continuous polarization. For MDEA, the potential during pulse mode 2 rapidly deteriorated and became extremely unstable upon the onset of carbonate salt precipitation.

Anodic chronopotentiometry results for the various pulse strategies are shown in Figure 5. Three distinct behaviours emerged: stable, erratic, and decreasing. A stable potential was noted in all specimens subjected to pulse mode 1, as well as in MEA under pulse mode 2. The potential required to reach a current density of +1 mA cm^-2 hovered around -0.15 V for pulse mode 1 and -0.2 V for pulse mode 2 in MEA. This variance is attributed to surface charging/discharging phenomena, necessitating more anodic potentials to offset the declining discharging current with an elevated Faradaic oxidation current for longer anodic durations. Since pulse mode 2 features shorter durations, the proportion of Faradaic current is reduced, hence less anodic potentials are sufficient to sustain the target current density.

In the case of MDEA and AMP under pulse mode 2, the anodic potential exhibited instability, albeit with markedly different behaviours. In MDEA using pulse mode 2, an erratic potential was observed beyond 15 hours, likely caused by the intermittent formation and detachment of carbonate salts on the catalyst surface. In contrast, AMP during pulse mode 2 exhibited a continuous cathodic shift in anodic potential over time.

The post-chronopotentiometry visual appearance of copper catalysts exhibits marked variations contingent on the polarization mode, as illustrated in Figure 6. Continuously polarized specimens display darker surfaces, whereas those subjected to pulse modes generally manifest ‘cleaner’ copper surfaces, with the exception of AMP under pulse mode 2. When correlating the visual observations of the catalysts post-chronopotentiometry with the anodic potential data from Figure 5, it becomes evident that periodic oxidation facilitated by pulse modes effectively mitigates the formation of dark deposits. The pronounced dark deposit observed in AMP under pulse mode 2 indicates inadequate oxidation of the copper catalyst. Indeed, several factors can contribute to an cathodic shift in potential when maintaining a target anodic current density, such as a reduction in active surface area, a shift in oxidation onset potential, or an increased charging of the interface reducing the proportion of Faradaic currents required to achieve the target. The observed potential diminution for AMP pulse mode 2 is presumably attributed to the latter, as post-test surface characterization revealed a dark deposit akin to that observed following continuous polarization, as shown in Figure 6. This suggests that the intended oxidation of copper was not effectively achieved, pointing to surface charging as the underlying cause for the diminished oxidation. Under these specific test conditions, an anodic duration of 2 seconds proved insufficient for achieving copper oxidation in CO₂-rich AMP. These findings underscore the importance of cyclic copper oxidation in preventing the formation of such dark deposits.

Artefacts resulting from gas generation at the catalyst surface, characterized by black spots with occasional dark trails directed upward, are discernible in specimens under continuous and pulse mode 1 polarization. However, these artefacts are absent in samples subjected to pulse mode 2, where no such phenomena are observed.

Higher magnification images of the catalyst surface are provided in Figure 7. Prior to chronopotentiometry, as shown in Figure 7a,b, the surface primarily consists of pure copper, characterized by an uneven topology with sporadic overgrown protrusions, ranging from 15 µm to 35 µm in diameter. Post-continuous polarization, the formation of a dark deposit is apparent, leaving only a thin network of exposed copper (Figure 7c,d). Conversely, in MEA under pulse mode 2 (Figure 7e), the surface displays no discernible dark deposits, and the integrity of the surface is notably preserved. An instance of the gas generation artefact, observable in MEA under pulse mode 1 (Figure 7f), exhibits a dark deposit in the shape of a ring, approximately 100 µm in diameter, with a centre of exposed copper corresponding to the cathodic site.

4. Discussion

4.1. Corrosion of Copper Catalyst in Amine Media

Corrosion rates were calculated from the corrosion current density (j_corr) in accordance with ASTM G102 guidelines [40]. The derived corrosion rates, along with the time necessary to dissolve a 50 µm copper deposit (the estimated thickness based on weight measurements), are tabulated in Table 2. These calculations reveal that the complete dissolution of the copper deposit, under the presumption of exclusive Cu(I) formation and in the absence of any passivation, would necessitate 56 days in the most severe scenario (CO₂-enriched MEA). In the case of Cu(II) formation, the time extends to 112 days. It is critical to recognize that the hypothesis of no passivation is valid only immediately after the termination of cathodic current, as an oxide protective layer is expected to form subsequently. Thus, these calculations are pertinent mainly for approximating the cumulative switch-off duration tolerable by the catalyst. Accordingly, a cumulative switch-off time threshold of 56 days is considered more than adequate. Therefore, free corrosion of copper in the amine media does not constitute a limiting factor for the catalyst's operational lifespan.

The influence of corrosion-induced surface alterations on the catalyst's efficiency, including aspects such as selectivity, FE, and EE, still requires further investigation. However, existing literature, including findings by [41], indicates that copper oxides favour the reduction of CO₂ into C₂+ products, suggesting that corrosion may not pose immediate concerns for catalyst functionality.

3.3. Choice of Amine Capture Media for ECR

CO₂ capture in amine media is primarily governed by two processes. The initial process involves the formation of carbamate, as described by reaction (1). Subsequently, the formed carbamate undergoes hydrolysis into bicarbonate, delineated in reaction (2). The prevalence of these reactions is contingent on the amine type. Non-sterically hindered primary amines, such as MEA, tend to form stable carbamate; thus, reaction (1) predominates, leading to almost complete CO₂ capture in the form of carbamate [42]. While this mechanism offers rapid capture kinetics, it necessitates higher energy for CO₂ release.

In sterically hindered amines like AMP, the carbamate bond is less stable [36,43], enhancing the carbamate hydrolysis reaction (reaction 2). This results in CO₂ being stored as both carbamate and bicarbonate, combining the fast capture kinetics of reaction (1) with an increased CO₂ absorption capacity due to the 1:1 stoichiometry between CO₂ and the amine molecule in reaction (2), in contrast to the 2:1 ratio in reaction (1).

$${CO}_2+2R_1{R}_{2}NH \rightleftharpoons R_1{R}_2{N}^{+}{H}_2$$

(1)

$$R_1{R}_2{N}^{+}{H}_2+H_{2}O\rightleftharpoons R_1{R}_{2}NH+HC{O}_3^{-}$$

(2)

Tertiary amines, such as MDEA, do not form carbamate with CO₂. Instead, they function as catalysts for CO₂ hydration [44], leading to exclusive bicarbonate capture as per reaction (3). This mechanism offers a higher absorption capacity, albeit at a slower capture rate.

$${C{O}_2+H_{2}O+R}_1{R}_2{R}_{3}N \rightleftharpoons HC{O}_3^{-}+R_1{R}_2{R}_3{N}^{+}H$$

(3)

Historically, capturing CO₂ as bicarbonate has been favourable due to its greater absorption capacity and reduced thermal energy requirement for CO₂ release. The findings presented here indicate that tertiary amine can lead to significant carbonate salt precipitation during ECR, as observed in MDEA and MDEA/PZ. In contrast, primary amine do not facilitate carbonate salt formation, as evidenced in MEA and AMP. Based on these observations, primary amines are emerging as more promising candidates for direct ECR applications. This is confirmed by chronopotentiometry results which showed greater stability for MEA.

3.3. Pulse ECR in Amine Media

Pulse chronopotentiometry findings clearly demonstrate that incorporating short anodic segments counteracts the cathodic shift in potential over time, often resulting in an anodic shift in cathodic potentials. This trend suggests an enhancement in the efficiency of reduction reactions, as evidenced by lower overpotentials needed to maintain the target current density. The formation of copper oxides during anodic segments is likely responsible for this anodic potential shift.

Beyond the advantageous potential shift, pulse ECR exhibits a pronounced ability to preserve the catalyst surface, effectively minimizing the formation of dark deposits. These outcomes highlight the necessity for optimization in pulse ECR to enhance results, such as maximizing potential shifts and reducing deposit formation, as exemplified by pulse mode 2 in MEA. The optimization process varies with the media used, as evidenced by the differences in outcomes for MEA and AMP under pulse mode 2. Key considerations for effective pulse ECR include ensuring adequate oxidation of the copper surface by setting a sufficiently long anodic step duration, counter to the approach seen in AMP under pulse mode 2. Additionally, the cathodic step duration should be short enough to prevent excessive deposit formation at gas generation sites, such as observed in AMP under pulse mode 1, which could be problematic to eliminate during subsequent anodic steps.

Carbonate salt formation arises from localized HO^- ion enrichment near the catalyst surface, a byproduct of the CO₂ reduction reaction (CO₂RR) [20]. Previous studies have suggested that pulse ECR can mitigate carbonate salt formation by curbing HO^- accumulation [21,29]. However, the pulse strategies evaluated were ineffective in preventing carbonate salt precipitation in MDEA-based capture media. This outcome implies that tertiary amines favour carbonate salt formation.

5. Conclusions

The investigation into the stability of electrodeposited copper catalysts for Electrochemical Reduction (ECR) in various amine media offers valuable insights into critical aspects of this process. The study underscores several key findings that advance our understanding and pave the way for future research endeavours:

• Corrosion is not a significant impediment to the catalyst's longevity in amine media. Both computational modelling and experimental data corroborate that the inherent corrosion of copper in these conditions does not critically limit the operational lifespan of the catalyst. This insight alleviates concerns regarding the durability of copper catalysts in practical ECR applications.
• Primary amines, particularly MEA, demonstrate a higher compatibility with ECR processes, characterized by the absence of carbonate salt precipitation and more stable potentials over time. This observation emphasizes the importance of considering the amine type in optimizing ECR performance and underscores the potential for tailored catalyst-amine combinations to improve efficiency.
• Pulse ECR demonstrated significant potential in improving ECR stability, manifested by a shift in cathodic potential and effective mitigation of deposit on the catalyst surface through periodic oxidation. This highlights the importance of exploring innovative operational strategies to augment the stability and efficiency of ECR processes.

Future investigations should prioritize delineating the specific products formed from the reduction of amine-carbamate adducts using electrodeposited copper catalysts. Understanding these reaction pathways is paramount for optimizing the ECR processes and expanding their industrial applications. Additionally, the effect of pulse strategies on ECR productivity needs exploration, particularly in understanding how the intermittent nature of these strategies influences the rate and efficiency of CO₂ conversion.