首页> 外文期刊>Journal of CO2 Utilization >CO2 reforming with methane for syngas production using a dielectric barrier discharge plasma coupled with Ni/gamma-Al2O3 catalysts: Process optimization through response surface methodology
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CO2 reforming with methane for syngas production using a dielectric barrier discharge plasma coupled with Ni/gamma-Al2O3 catalysts: Process optimization through response surface methodology

机译:使用介电阻挡放电等离子体与Ni / Gamma-Al2O3催化剂耦合的甲烷改性合成气的二氧化碳改性:通过响应表面方法处理优化

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In this work, CO2 reforming with methane in the form of biogas over Ni/gamma-Al2O3 catalysts was carried out in a coaxial dielectric barrier discharge (DBD) non-thermal plasma reactor. The effects of various process parameters (biogas flow rate, discharge power, CO2/CH4 molar ratio and Ni loading) and their interactions on the hybrid plasma-catalytic biogas reforming were evaluated using response surface methodology through a four-factor, five-level central composition design. Quadratic regression models were developed to gain a better understanding of the relationships between these process parameters (independent variables) and the biogas conversion, syngas yield and energy efficiency (responses) of the plasma reforming process. The results indicated that biogas flow rate was the most significant factor affecting the conversion of CO2 and CH4 and syngas yield, while the CO2/CH4 molar ratio was the leading process parameter determining the energy efficiency of the process. In addition, there was a trade-off between the biogas conversion and energy efficiency of the process at different specific energy inputs (SEI). The process optimization suggested that the optimal process performance was achieved at a biogas flow rate of 56.1 ml/min, a discharge power of 60.0 W, a CO2/CH4 molar ratio of 1.03 and a Ni loading of 9.5 wt.%, which was demonstrated by the reproducibility of the experimental results. Moreover, the carbon deposition on the spent catalyst was only 3.9% after running the plasma biogas reforming process for 150 min under the optimal experimental conditions.
机译:在这项工作中,在同轴介电阻挡放电(DBD)非热等离子体反应器中,在同轴介电阻挡放电(DBD)非热等离子体反应器中,用沼气形式的CO2与沼气形式的重整。通过四因素,五级中央评估各种工艺参数(沼气流量,放电功率,CO2 / CH4摩尔比和Ni负载)的影响及其对杂交血浆催化沼气重整的它们对杂化等离子体催化沼气重整的相互作用组成设计。开发了二次回归模型,以更好地了解这些过程参数(独立变量)与沼气转换,Syngas产量和能效(响应)之间的关系的关系更好地理解等离子体重整过程的关系。结果表明,沼气流量是影响CO 2和CH4和合成气产量的转化的最显着因素,而CO2 / CH4摩尔比是确定该过程的能量效率的前导过程参数。此外,在不同特定能量投入(SEI)的过程的沼气转换和能效之间存在权衡。该过程优化表明,最佳过程性能以56.1mL / min的沼气流速实现,放电功率为60.0W,CO 2 / CH 4摩尔比为1.03,Ni负载量为9.5重量%,表明通过实验结果的再现性。此外,在最佳实验条件下,在运行血浆沼气重整过程150分钟后,废催化剂上的碳沉积仅为3.9%。

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