验证亚大气压微波气体放电中二氧化碳转化建模的热化学方法

Vladislav Kotov, C. Kiefer, Ante Hecimovic
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摘要

CO2→CO+½O2 转换实验 [F~A~D'Isa 等人,2020 等离子体源科学与技术,29 105009] 与热化学计算进行了比较。该实验采用 2.45 GHz 等离子体炬,流出物为直通道。CO2/CO/O2/O/C 混合物的 1.5D 模型没有湍流传输,等离子体仅作为规定热源。参数范围为:压力 p=0.9 巴时,比能量输入(SEI)为 0.3-5 eV/分子;压力 p=0.5 和 0.2 巴时,比能量输入(SEI)为 0.6-2 eV/分子。计算出的转化率 χ 始终接近实验值。同时,计算得到的温度 T 与实验值偏差很大,尤其是在 p=0.2 巴时。计算得出的 T 对不确定的模型参数也很敏感,但 χ 并不敏感。根据模型,净转换主要是由 CO 和 O 从热核向壁的径向扩散以及陡峭的径向温度梯度驱动的。降低能量效率的主要因素是热等离子体区域边缘和下游 CO 的再氧化。模型中的净转换在很大程度上是由 CO 和 O 从热核向壁面的径向扩散以及陡峭的径向温度梯度驱动的。降低能量效率的主要因素是 CO 在热等离子体区域边缘和下游的再氧化。所采用的 1.5D 近似方法有一个原则性的限制,即无法研究现实的大体流场对化学过程的影响。因此,必须将这些结果视为初步结果,并通过对反应器内的涡流稳定流建立更复杂、更精确的模型来加以证实。
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Validation of the thermo-chemical approach to modelling of the CO2 conversion in sub-atmospheric pressure microwave gas discharges
The CO2→CO+½O2 conversion experiment [F~A~D’Isa et al. 2020 Plasma Sources Sci. Technol. 29 105009] has been compared with thermo-chemical calculations. The experiment is a 2.45 GHz plasma torch with straight channel in the effluent. The 1.5D model of the CO2/CO/O2/O/C mixture without turbulent transport has been applied with plasma acting only as prescribed heat source. The parameter range covered is specific energy input (SEI) 0.3-5 eV/molecule at pressure p=0.9 bar, and SEI=0.6-2 eV/molecule at p=0.5, 0.2 bar. The calculated conversion χ is always close to experimental values. At the same time, the calculated temperatures T deviate significantly from the experiment, especially for p=0.2 bar. The calculated T were also found to be sensitive with respect to the uncertain model parameters, but χ is not sensitive. According to the model the net conversion is driven mainly by the radial diffusion of CO and O from the hot core toward the wall and steep radial temperature gradients. The main factor which reduces the energy efficiency is re-oxidation of CO at the edge of the hot plasma region and downstream. The net conversion in the model is driven to large extent by the radial diffusion of CO and O from the hot core toward the wall and steep radial temperature gradients. The main factor which reduces the energy efficiency is re-oxidation of CO at the edge of the hot plasma region and downstream. The 1.5D approximation applied has the principle limitation that the impact of the realistic bulk flow field on the chemical process could not be studied. Hence the results must be considered as preliminary and have to be confirmed with a more elaborate and accurate model of the vortex stabilized flows inside the reactor.
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