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    旋转滑动弧等离子体耦合水冷促进CO2转化

    CO2 conversion promoted by water-cooling coupled with rotating gliding arc plasma

    • 摘要: CO2的捕集、利用与封存被广泛认为是碳减排的主要技术路线之一,也是我国应对“双碳”目标挑战的重要手段。滑动弧放电等离子体具有能量效率高、结构简单、启停时间短、耗能低等优点,在CO2转化利用中是极具潜力的技术手段。然而,滑动弧等离子体在活化分解CO2过程中存在气体温度过高(40006000 K),加剧CO2分解逆反应进行问题,导致转化率受限。为此,开发了一种水冷旋转滑动弧等离子体反应器,创新性地利用冷却抑制CO2分解逆反应机制有效提升CO2转化效果,并探讨了不同水冷强度下的CO2分解反应行为。通过对等离子体下游的气体温度进行测量,确定了不同冷凝强度及不同工况下的等离子体宏观气体温度变化情况,系统考察了进气流量(2~8 L/min)和冷却强度对水冷反应器中CO2分解转化率和能量效率的影响。结果表明,水冷的引入显著降低了反应区的气体温度,抑制了高温导致的CO2逆反应,从而提高了CO2转化率和能量效率。在无水冷条件下,气体温度达到461 ℃,而中等和强水冷下分别降低至282 ℃和222 ℃。此外,水冷系统的加入将反应器的稳定时间从400 s降低到150 s,并提高了反应的稳定性。水冷的加入显著降低了CO2分解逆反应的速率,由于VT弛豫过程得以抑制,振动激发能级能量水平得以提高,因此CO2转化效果得以提高。最佳实验工况为中等水冷强度(冷却水流量4.8 mL/s)和进气流量4~5 L/min,此条件下可获得较高的CO2转化率(9.5%~11.5%)和能量效率(26.0%~29.5%)。证明了水冷在抑制高温逆反应、提高CO2转化性能中的有效性,为等离子体CO2转化技术的进一步发展提供了新的思路。

       

      Abstract: CO2 capture, utilization, and storage are widely regarded as one of the main technological pathways for carbon reduction, and an important method for China to address the challenges of its "dual carbon" goals. Rotating gliding arc plasma possesses advantages such as high energy efficiency, simple structure, short start-up and shut-down times, and low energy consumption, making it a highly promising technology for CO2 conversion and utilization. However, during the activation and decomposition of CO2, rotating gliding arc plasma experiences excessively high gas temperatures (40006000 K), which exacerbates the reverse reaction of CO2 decomposition, limiting the conversion rate. To address this, a water-cooled rotating sliding arc plasma reactor has been developed in this study. This innovative approach utilizes cooling to suppress the mechanism of the reverse reaction of CO2 decomposition, effectively enhancing CO2 conversion efficiency. The study explores the decomposition behavior of CO2 under different cooling intensities. By measuring the gas temperature downstream of the plasma, variations in the macro gas temperature under different condensation intensities and operating conditions were determined. The effects of inlet gas flow rate (2−8 L/min) and cooling intensity on CO2 decomposition conversion rate and energy efficiency within the water-cooled reactor were systematically investigated. The experimental results indicate that the introduction of water cooling significantly lowers the gas temperature in the reaction zone, suppressing the reverse reaction of CO2 caused by high temperatures, thereby increasing both CO2 conversion rates and energy efficiency. In the absence of water cooling, the gas temperature reached 461 °C, whereas under moderate and strong water cooling conditions, it was reduced to 282 °C and 222 °C, respectively. Additionally, the introduction of the water cooling system reduced the stability time of the reactor from 400 s to 150 s, enhancing the stability of the reaction. The introduction of water cooling significantly decreased the rate of the reverse reaction of CO2 decomposition. Due to the suppression of the vibration-translation relaxation process, the energy levels of vibrationally excited states were elevated, thus enhancing CO2 conversion efficiency. The optimal experimental conditions were found to be with medium cooling intensity (cooling water flow rate of 4.8 mL/s) and an inlet gas flow rate of 4−5 L/min, under which a high CO2 conversion rate (9.5%−11.5%) and energy efficiency (26.0%−29.5%) were achieved. This study demonstrates the effectiveness of water cooling in suppressing high-temperature reverse reactions of CO2 conversion and improving CO2 conversion performance, providing new insights for the further development of plasma CO2 conversion technologies.

       

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