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非平衡态等离子体催化CO2加氢逆水煤气反应的实验研究

Experimental Study on Non-equilibrium Plasma-catalyzed Reverse Water-gas Shift Reaction for CO2 Hydrogenation

  • 摘要: 本文采用非平衡态等离子体放电技术协同Cu基催化剂的方法,促进CO2加氢逆水煤气反应低温高效地进行。实验对比分析了纯催化、纯等离子体以及二者协同作用下对CO2转化性能的影响,重点考察了等离子体放电电压、气体流量、CO2和H2的比例、循环水温度对CO2转化率、CO选择性的影响,以及不同条件下的SEI值和能量效率。结果表明,等离子体放电与催化剂协同作用效果显著,在放电电压为16 kV,气体流量为20 mL/min,CO2:H2=1:3,循环水温度为80℃时,CO2的转化率高达79.17%,CO选择性达到50.83%。在CO2:H2比例为1:1、1:2以及60−90 mL/min的大流量条件下能量效率较高,最高可达208.47 µmol/kJ。

     

    Abstract: This study employs a non-equilibrium plasma discharge technology combined with Cu-based catalysts to enhance the low-temperature efficiency of CO2 hydrogenation via the reverse water-gas shift (RWGS) reaction. The experiment compared and analyzed the effects of catalysis, plasma, and their synergistic effects on CO2 conversion performance, focusing on the effects of plasma discharge voltage, gas flow rate, CO2 and H2 ratio, circulating water temperature on CO2 conversion rate and CO selectivity, as well as SEI values and energy efficiency under different conditions. The results showed that the synergistic effect of plasma discharge and catalyst was significant. At a discharge voltage of 16 kV, gas flow rate of 20 mL/min, CO2:H2=1:3, and circulating water temperature of 80℃, the conversion rate of CO2 reached 79.17%, and the selectivity of CO reached 50.83%. Under high flow conditions with CO2:H2 ratios of 1:1 or 1:2, and 60−90 mL/min, the energy efficiency is relatively high, reaching up to 208.47 µmol/kJ.

     

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