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    电催化还原CO2制合成气传质过程模拟及催化剂结构优化

    Simulation of mass transfer process and optimization of catalyst structure for syngas production by electrocatalytic reduction of CO2

    • 摘要: 电催化二氧化碳还原反应(CO2RR)是应对全球气候变化和实现能源转型的关键技术之一。通过将CO2转化为有价值的化学品,可以有效地减少温室气体排放并为可持续能源的开发提供动力。CO2RR过程中常常伴随析氢反应(HER)发生,生成H2与CO行成合成气。合成气的H2与CO比例对下游化学品的合成具有重要影响。因此,调控催化剂的厚度和孔隙率等结构,是实现目标产物精确控制的有效途径之一。Ni−N−C催化剂以其对CO产物的高选择性,在电催化合成气制备过程中,尤其是在合成气比例n(H2)/n(CO)为0.5~5范围内表现出显著优势。研究采用有限元数值模拟方法,构建了二维膜电极电解槽(MEA)模型,探讨了Ni−N−C催化剂厚度与孔隙率对MEA中的传质、CO2RR及HER反应选择性和产物浓度分布的影响。通过对催化剂厚度5~95 μm和孔隙率0.2~0.9的进行模拟,发现随着催化剂厚度从65 μm增加到95 μm,CO2的扩散效果逐渐增强,限制了CO浓度的提高,从而影响合成气的比例,在电压为2.5~3.1 V范围内,合成气的比例稳定在1~5。另一方面,提高催化剂的孔隙率,特别是在0.2~0.9的范围内,有助于缓解CO2扩散对反应速率的限制,从而提升CO产物的浓度。在1.6~2.2 V的低电压范围内,能够制备得到比例为0.5~1的合成气。研究为MEA中催化剂的设计和优化提供了理论支持,能够为未来电催化CO2还原反应的工业应用提供指导。

       

      Abstract: Electrocatalytic carbon dioxide reduction reactions (CO2RR) are one of the key technologies for addressing global climate change and achieving energy transition. By converting CO2 into valuable chemicals, greenhouse gas emissions can be effectively reduced, and sustainable energy development can be promoted. Hydrogen evolution reactions (HER) often occur during CO2RR, producing H₂ and CO to form syngas. The H2 to CO ratio in syngas significantly influences the synthesis of downstream chemicals. Therefore, regulating the structure of the catalyst, such as its thickness and porosity, is an effective approach to achieving precise control of target products. Ni−N−C catalysts, with their high selectivity for CO products, demonstrate significant advantages in the electrocatalytic syngas production process, particularly within the syngas ratio range of 0.5 to 5. The study employed finite element numerical simulation methods to construct a two-dimensional membrane electrode assembly (MEA) model, investigating the effects of Ni−N−C catalyst thickness and porosity on mass transfer, CO2 reduction reaction (CO2RR), hydrogen evolution reaction (HER) selectivity, and product concentration distribution within the MEA. Simulations were conducted for catalyst thicknesses ranging from 5 to 95 μm and porosities from 0.2 to 0.9. It was found that as the catalyst thickness increased from 65 μm to 95 μm, CO2 diffusion gradually enhanced, limiting the increase in CO concentration and thereby affecting the syngas ratio. Within the voltage range of 2.5 V to 3.1 V, the syngas ratio remained stable between 1 and 5. On the other hand, increasing the catalyst porosity, particularly within the range of 0.2 to 0.9, helps alleviate the diffusion-induced rate limitation of CO2, thereby enhancing the concentration of CO products. Within the low voltage range of 1.6 V to 2.2 V, syngas with a ratio of 0.5 to 1 can be produced. This study provides theoretical support for the design and optimization of catalysts in MEA systems, offering guidance for future industrial applications of electrocatalytic CO2 reduction reactions.

       

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