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采用混合表面/填充床放电等离子体实现苯的降解的创新方法。

Innovative approach for benzene degradation using hybrid surface/packed-bed discharge plasmas.

机构信息

Institute of Electrostatics and Special Power, Dalian University of Technology , Dalian 116024, People's Republic of China.

出版信息

Environ Sci Technol. 2013 Sep 3;47(17):9898-903. doi: 10.1021/es401110h. Epub 2013 Aug 20.

Abstract

An innovative plasma reactor, which generates hybrid surface/packed-bed discharge (HSPBD) plasmas, was employed for the degradation of benzene. The HSPBD reactor was found to display remarkably better benzene degradation, mineralization, and energy performance than surface or packed-bed discharge reactors alone. The degradation efficiency, CO2 selectivity, and energy yield in the HSPBD reactor were 21%, 11%, and 3.9 g kWh-1 higher, respectively, than in a surface discharge reactor and 30%, 21%, and 5.5 g kWh-1 higher, respectively, than in a packed-bed discharge reactor operated at 280 J L-1. Particularly, the benzene degradation in the HSPBD reactor exhibited an unambiguous synergistic enhancement rather than a simple additive effect using the surface discharge and packed-bed discharge reactors. Moreover, in the HSPBD reactor, the formation of byproducts, such as NO2, was suppressed, while O3 was promoted. The use of N2 as the carrier gas was found to be effective for benzene degradation because of the fast reaction rate of N2(A3∑u+) with benzene, and oxygen species derived from the dissociation of O2 were found to be significant in the mineralization process. Thus, the addition of O2 to N2 allows for efficient degradation of benzene, and the optimized amount of O2 was determined to be 3%.

摘要

一种创新性的等离子体反应器,能够产生混合表面/填充床放电(HSPBD)等离子体,被用于苯的降解。与单独的表面放电或填充床放电反应器相比,HSPBD 反应器显示出明显更好的苯降解、矿化和能量性能。在 HSPBD 反应器中,降解效率、CO2 选择性和能量产率分别比表面放电反应器高 21%、11%和 3.9 g kWh-1,比填充床放电反应器高 30%、21%和 5.5 g kWh-1,而后者的操作能量密度为 280 J L-1。特别地,与使用表面放电和填充床放电反应器的简单加和效应相比,HSPBD 反应器中的苯降解表现出明确的协同增强效应。此外,在 HSPBD 反应器中,抑制了副产物(如 NO2)的形成,而促进了 O3 的形成。使用 N2 作为载气被发现对苯的降解有效,因为 N2(A3∑u+)与苯的快速反应速率,以及 O2 分解产生的含氧物种在矿化过程中具有重要意义。因此,向 N2 中添加 O2 可以实现苯的有效降解,并且确定最佳的 O2 量为 3%。

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