Acceleration of the reduction of carbon dioxide in the presence of multivalent cations
Introduction
The electrochemical reduction of CO2 was studied for the first time in 1870 by Royer [1]. Since then, it has been the subject of a large number of publications, especially during the recent twenty years. These works have been reviewed by Sammells and Cook [2], Jitaru et al. [3], Hori [4], Gattrell et al. [5] as well as by Chaplin and Wragg [6].
The conversion of CO2 to organic chemicals is of crucial importance for the storage of the energy produced by renewable energy sources such as wind, solar, geothermal as well as from nuclear stations. Among various chemicals that can be produced from the reduction of CO2, methanol has many advantages. The “methanol economy” in which methanol will replace fossil fuels is an alternative way to the so-called “hydrogen economy” due to the limitations and disadvantages of hydrogen [7]. Even though the electrochemical production of methanol from CO2 is thermodynamically more favorable than the production of hydrogen from water [8], which is the main competitive reaction, it is kinetically difficult and needs suitable electrocatalysts and reaction conditions. Formation of methanol has been observed on various metallic electrodes such as Ru [9], Mo [10], Cu (90.5)–Ni (9.5) [11], Cu in a C2H5OH–H2O–LiCl electrolyte [12] and on Ru–Cu [13] as well as on conductive oxides such as RuO2 [14] or mixtures of oxides [8]. The % CE usually is high at low cathodic overpotentials and depends strongly on the nature of the cathode and the other electrolysis conditions.
The influence of the electrolyte and its concentration on the electrochemical reduction of CO2 has been studied in several works [14], [15], [16], [17], [18], [19], [20], [21], [22]. It has been found from steady state electrolytic experiments that the rate of the reduction depends on the Stokes radius of the alkali metal cation in the order Li+ < Na+ < K+ < Cs+. Cyclic voltammetry experiments have also proved that the rate of the reduction increases as the size of the anion of the electrolyte increases in the order Cl− < Br− < I− [23].
The present work includes experimental results on the influence of multivalent cations on the rate of the reduction of CO2. The effect of the halogen anions and the acidity of the electrolyte was also studied.
Section snippets
Experimental
A Teflon cell having a total volume of 24 mL (Scheme 1) was used in all experiments. A Nafion 117 (H+ form) cation exchange membrane divided the cell into two equal volume compartments. The heat transfer from the cell was achieved by two aluminum plates (10 cm × 10 cm × 0.5 cm). The compartment of the catholyte had an extra volume of 2 mL on the top, in order to secure that the electrolyte covered the whole surface of the cathode, despite the volume removed due to the sampling. Moreover, the cell had an
Influence of the potential
Fig. 1 shows the cyclic voltammograms of the supporting electrolyte (1.5 mol L−1 HCl, 0.5 mol L−1 NaCl) as well as that of a CO2 saturated solution. The current density in the presence of CO2 was lower than that of the background electrolyte in all the potential range examined and this is in accordance with a previous work [21]. This was attributed to the inhibition of the hydrogen evolution reaction from the adsorbed CO2 or from intermediates of the reduction.
Fig. 2a shows that the current density
Conclusions
The rate of the reduction of carbon dioxide at low overpotentials, where the rate determining step is the reduction of the negatively charged anion (CO2−) increases as the surface charge of the cation of the supporting electrolyte increases from Na+ to La3+ in strongly acidic solution and this increase is more intense at pH > 4. The influence of the cation is minimized at high overpotentials, because the rate determining step of the reduction changes. The halogen anion increases the rate in the
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