Review of packed-bed plasma reactor for ozone generation and air pollution control

被引:167
作者
Chen, Hsin Liang [1 ]
Lee, How Ming [2 ]
Chen, Shiaw Huei [2 ]
Chang, Moo Been [1 ]
机构
[1] Natl Cent Univ, Grad Inst Environm Engn, Tao Yuan 32001, Taiwan
[2] Inst Nucl Energy Res, Environm & Energy Technol Ctr, Div Phys, Tao Yuan 62546, Taiwan
关键词
D O I
10.1021/ie071411s
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Packed-bed plasma reactors, constructed by packing noncatalytic dielectric pellets inside nonthermal plasma reactors, have been demonstrated to effectively alleviate the major bottleneck encountered by nonthermal plasma, i.e., the energy efficiency needs to be further improved. As far as the environmental issues are concerned, packed-bed plasma reactors are mainly applied to ozone generation and gaseous pollutant removal. According to the available experimental data, for a given specific energy density, the energy efficiency for ozone generation and gaseous pollutant abatement obtained with packed-bed reactors, if compared to that of nonpacked reactors, could be 1.1-4.3 and 1.1-12 times higher, depending on the type of pollutant, the reactor geometry, and the packing pellets used. Nevertheless, it is worth noticing that the packing pellets suitable for ozone generation and pollutant removal are quite different. The influences of material, dielectric constant, size, and shape of the packing pellets on the performance for ozone generation and gaseous pollutant removal are comprehensively reviewed in this paper and guidelines for pellet selection are provided as well. For the single-stage plasma catalysis system, in which catalyst pellets are directly packed inside the plasma reactor, the physical parameters of catalyst would also have significant influence on the plasma characteristics and the performance. Therefore, the content of this review paper could provide useful information for single-stage plasma catalysis system from the viewpoint of plasma characteristics.
引用
收藏
页码:2122 / 2130
页数:9
相关论文
共 73 条
[1]   Decomposition of toluene and acetone in packed dielectric barrier discharge reactors [J].
Chang, CL ;
Lin, TS .
PLASMA CHEMISTRY AND PLASMA PROCESSING, 2005, 25 (03) :227-243
[2]  
Chang J. S., 1998, P C EL INS DIEL PHEN, P485
[3]   Removal of NF3 from semiconductor-process flue gases by tandem packed-bed plasma and adsorbent hybrid systems [J].
Chang, JS ;
Kostov, KG ;
Urashima, K ;
Yamamoto, T ;
Okayasu, Y ;
Kato, T ;
Iwaizumi, T ;
Yoshimura, K .
IEEE TRANSACTIONS ON INDUSTRY APPLICATIONS, 2000, 36 (05) :1251-1259
[4]  
CHANG JS, 1997, J ADV OXID TECHNOL, V2, P346
[5]   Abatement of perfluorocarbons with combined plasma catalysis in atmospheric-pressure environment [J].
Chang, MB ;
Lee, HM .
CATALYSIS TODAY, 2004, 89 (1-2) :109-115
[6]   Simultaneous removal of nitrogen oxide/nitrogen dioxide/sulfur dioxide from gas streams by combined plasma scrubbing technology [J].
Chang, MB ;
Lee, HM ;
Wu, FL ;
Lai, CR .
JOURNAL OF THE AIR & WASTE MANAGEMENT ASSOCIATION, 2004, 54 (08) :941-949
[7]   Enhancement of energy yield for ozone production via packed-bed reactors [J].
Chen, HL ;
Lee, HM ;
Chang, MB .
OZONE-SCIENCE & ENGINEERING, 2006, 28 (02) :111-118
[8]  
Cooper C.D., 2002, AIR POLLUT CONTROL, V4th
[9]   Removal of formaldehyde from gas streams via packed-bed dielectric barrier discharge plasmas [J].
Ding, HX ;
Zhu, AM ;
Yang, XF ;
Li, CH ;
Xu, Y .
JOURNAL OF PHYSICS D-APPLIED PHYSICS, 2005, 38 (23) :4160-4167
[10]   Performance evaluation of a hybrid system comprising silent discharge plasma and manganese oxide catalysts for benzene decomposition [J].
Einaga, H ;
Ibusuki, T ;
Futamura, S .
IEEE TRANSACTIONS ON INDUSTRY APPLICATIONS, 2001, 37 (05) :1476-1482