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Carbon Dioxide and Water Electrolysis Using New Alkaline Stable Anion Membranes

机译:使用新型碱性稳定阴离子膜的二氧化碳和水电解

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The recent development and market introduction of a new type of alkaline stable imidazole-based anion exchange membrane and related ionomers by Dioxide Materials is enabling the advancement of new and improved electrochemical processes which can operate at commercially viable operating voltages, current efficiencies, and current densities. These processes include the electrochemical conversion of CO2 to formic acid (HCOOH), CO2 to carbon monoxide (CO), and alkaline water electrolysis, generating hydrogen at high current densities at low voltages without the need for any precious metal electrocatalysts. The first process is the direct electrochemical generation of pure formic acid in a three-compartment cell configuration using the alkaline stable anion exchange membrane and a cation exchange membrane. The cell operates at a current density of 140 mA/cm2 at a cell voltage of 3.5 V. The power consumption for production of formic acid (FA) is about 4.3 - 4.7 kWh/kg of FA. The second process is the electrochemical conversion of CO2 to CO, a key focus product in the generation of renewable fuels and chemicals. The CO2 cell consists of a two-compartment design utilizing the alkaline stable anion exchange membrane to separate the anode and cathode compartments. A nanoparticle IrO2 catalyst on a GDE structure is used as the anode and a GDE utilizing a nanoparticle Ag/imidazolium-based ionomer catalyst combination is used as a cathode. The CO2 cell has been operated at current densities of 200 to 600 mA/cm2 at voltages of 3.0 to 3.2 respectively with CO2 to CO conversion selectivities of 95 - 99%. The third process is an alkaline water electrolysis cell process, where the alkaline stable anion exchange membrane allows stable cell operation in 1 M KOH electrolyte solutions at current densities of 1 A/cm2 at about 1.90 V. The cell has demonstrated operation for thousands of hours, showing a voltage increase in time of only 5 μV/h. The alkaline electrolysis technology does not require any precious metal catalysts as compared to polymer electrolyte membrane (PEM) design water electrolyzers. In this paper, we discuss the detailed technical aspects of these three technologies utilizing this unique anion exchange membrane.
机译:Dioxide Materials对新型碱性稳定的基于咪唑的阴离子交换膜和相关离聚物的最新开发和市场推广,使能够在商业上可行的工作电压,电流效率和电流密度下运行的新型电化学工艺得以发展。这些过程包括将CO2电化学转化为甲酸(HCOOH),将CO2转化为一氧化碳(CO)以及碱性水电解,从而在低压下以高电流密度产生氢,而无需任何贵金属电催化剂。第一个过程是使用碱性稳定的阴离子交换膜和阳离子交换膜在三室电池配置中直接电化学生成纯甲酸。电池在3.5 V的电池电压下以140 mA / cm2的电流密度工作。生产甲酸(FA)的功耗约为4.3-4.7 kWh / kg FA。第二个过程是将CO2电化学转化为CO,这是可再生燃料和化学品生产中的关键重点产品。 CO2电池由两室设计组成,利用碱性稳定的阴离子交换膜将阳极室和阴极室分隔开。 GDE结构上的纳米颗粒IrO2催化剂用作阳极,而利用纳米颗粒Ag /咪唑基离聚物催化剂组合的GDE用作阴极。 CO2电池的工作电流分别为200至600 mA / cm2,电压为3.0至3.2,CO2至CO的转化选择性为95%至99%。第三个过程是碱性水电解槽过程,其中碱性稳定的阴离子交换膜可在1 M KOH电解质溶液中以1. A / cm2的电流密度在1.90 V的电压下稳定运行。该电池已证明运行了数千小时,显示电压随时间仅增加了5μV/ h。与聚合物电解质膜(PEM)设计的水电解槽相比,碱性电解技术不需要任何贵金属催化剂。在本文中,我们将讨论利用这种独特的阴离子交换膜的这三种技术的详细技术方面。

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