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Process conditions for complete decomposition of CHF3 in a dielectric barrier discharge reactor

机译:CHF3在介电势垒放电反应器中完全分解的工艺条件

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摘要

Plasma decomposition of CHF3 was investigated using a dielectric barrier discharge immersed in an electrically insulating oil bath in a mixture of CHF3, O-2, and N-2. CHF3 was well decomposed under a relatively high applied voltage in an atmospheric pressure plasma system. The main by-product was CO2 and its selectivity increased with a decrease in the CHF3 concentration in the feed. Complete decomposition of CHF3 was achieved at a typical process range: an applied voltage a parts per thousand yen7.0 kVp, an initial CHF3 flow rate of 3ml/min, and a total flow rate of 500ml/min. The value of energy efficiency and energy density at the center range for the complete decomposition of CHF3 was 0.01 mmol/kJ and 6.00kWh/Nm(3), respectively.
机译:使用浸入CHF3,O-2和N-2混合物的电绝缘油浴中的介电势垒放电研究CHF3的等离子体分解。在大气压等离子体系统中,CHF3在较高的施加电压下能很好地分解。主要副产物为CO2,其选择性随进料中CHF3浓度的降低而增加。 CHF 3的完全分解在一个典型的工艺范围内实现:施加的电压为千分之几(7.0 kVp),初始CHF3流速为3ml / min,总流速为500ml / min。 CHF3完全分解的中心区域的能量效率和能量密度分别为0.01 mmol / kJ和6.00kWh / Nm(3)。

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