Lobaccaro Peter, Singh Meenesh R, Clark Ezra Lee, Kwon Youngkook, Bell Alexis T, Ager Joel W
Joint Center for Artificial Photosynthesis, Lawrence Berkeley National Laboratory, CA 94720, USA.
Phys Chem Chem Phys. 2016 Sep 29;18(38):26777-26785. doi: 10.1039/c6cp05287h.
In the last few years, there has been increased interest in electrochemical CO reduction (CO2R). Many experimental studies employ a membrane separated, electrochemical cell with a mini H-cell geometry to characterize CO2R catalysts in aqueous solution. This type of electrochemical cell is a mini-chemical reactor and it is important to monitor the reaction conditions within the reactor to ensure that they are constant throughout the study. We show that operating cells with high catalyst surface area to electrolyte volume ratios (S/V) at high current densities can have subtle consequences due to the complexity of the physical phenomena taking place on electrode surfaces during CO2R, particularly as they relate to the cell temperature and bulk electrolyte CO concentration. Both effects were evaluated quantitatively in high S/V cells using Cu electrodes and a bicarbonate buffer electrolyte. Electrolyte temperature is a function of the current/total voltage passed through the cell and the cell geometry. Even at a very high current density, 20 mA cm, the temperature increase was less than 4 °C and a decrease of <10% in the dissolved CO concentration is predicted. In contrast, limits on the CO gas-liquid mass transfer into the cells produce much larger effects. By using the pH in the cell to measure the CO concentration, significant undersaturation of CO is observed in the bulk electrolyte, even at more modest current densities of 10 mA cm. Undersaturation of CO produces large changes in the faradaic efficiency observed on Cu electrodes, with H production becoming increasingly favored. We show that the size of the CO bubbles being introduced into the cell is critical for maintaining the equilibrium CO concentration in the electrolyte, and we have designed a high S/V cell that is able to maintain the near-equilibrium CO concentration at current densities up to 15 mA cm.
在过去几年中,人们对电化学二氧化碳还原(CO₂R)的兴趣日益增加。许多实验研究采用具有微型H型电池几何结构的膜分离电化学电池,以表征水溶液中的CO₂R催化剂。这种类型的电化学电池是一个微型化学反应器,监测反应器内的反应条件以确保在整个研究过程中条件保持恒定非常重要。我们表明,在高电流密度下运行具有高催化剂表面积与电解液体积比(S/V)的电池可能会产生微妙的影响,这是由于CO₂R过程中电极表面发生的物理现象较为复杂,特别是与电池温度和本体电解液CO浓度有关的现象。使用铜电极和碳酸氢盐缓冲电解液在高S/V电池中对这两种影响进行了定量评估。电解液温度是通过电池的电流/总电压以及电池几何结构的函数。即使在非常高的电流密度20 mA/cm²下,温度升高也小于4℃,预计溶解的CO浓度降低<10%。相比之下,CO气液传质进入电池的限制产生的影响要大得多。通过使用电池中的pH值来测量CO浓度,即使在更适中的电流密度10 mA/cm²下,也观察到本体电解液中CO存在明显的不饱和状态。CO的不饱和状态会使在铜电极上观察到的法拉第效率发生很大变化,析氢变得越来越有利。我们表明,引入电池的CO气泡大小对于维持电解液中的平衡CO浓度至关重要,并且我们设计了一种高S/V电池,能够在高达15 mA/cm²的电流密度下维持接近平衡的CO浓度。