Degradation properties and mechanism of naphthalene from exhaust gas using dielectric barrier discharge
WU Zu-liang1, XIE De-yuan1, LU Hao1, YAO Shui-liang1, GAO Xiang2
1. College of Environmental Science and Engineering, Zhejiang Gongshang University, Hangzhou 310012, China; 2. State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027, China
Effects of the initial volume fraction of naphthalene, residence time and exhaust gas components on naphthalene degradation process were analyzed. The naphthalene degradation mechanism was explored through byproducts analysis. Degradation efficiency decreases with the increasing initial volume fraction, while the energy utilization efficiency improves. When the residence time is prolonged, the degradation efficiency trends to be stable, while the COx selection rate enhances step by step. The degradation efficiency can reach above 70% as the volume fraction of oxygen gas from exhausted gas is 3%, but the COx selection rate is only 30%. The degradation efficiency is relatively stable when the volume fraction of oxygen gas is 3%-20%, while the COx selection rate gradually increases and goes to 77% at 20% volume fraction of oxygen gas. According to the degradation byproducts, nitrogen gas excited state plays an important role during the initial degradation of naphthalene. And O radical can promote the naphthalene degradation through some direct collision reactions. However, complete degradation of naphthalene depends on O and OH radicals.
WU Zu-liang, XIE De-yuan, LU Hao, YAO Shui-liang, GAO Xiang. Degradation properties and mechanism of naphthalene from exhaust gas using dielectric barrier discharge. JOURNAL OF ZHEJIANG UNIVERSITY (ENGINEERING SCIENCE), 2014, 48(6): 1120-1126.
[1] ZHANG Y X, TAO S, SHEN H Z, et al. Inhalation exposure to ambient polycyclic aromatic hydrocarbons and lung cancer risk of Chinese population[J]. Proceedings of the National Academy of the Sciences of the United States of America, 2009, 106(50): 21063-21067.
[2] ZHANG Y X, TAO S. Global atmospheric emission inventory of polycyclic aromatic hydrocrbons (PAHs) for 2004[J]. Atmospheric Environment, 2009, 43(4): 812-819.
[3] ZHU L Z, LU H, CHEN S G, et al. Pollution level, phase distribution and source analysis of polycyclic aromatic hydrocarbons in residential air in Hangzhou, China[J]. Journal of Hazardous Materials, 2009, 162(2/3):1165-1170.
[4] YANG K, ZHU L Z, XING B S. Adsorption of polycyclic aromatic hydrocarbons by carbon nanomaterials[J]. Environmental Science & Technology, 2006, 40(6): 1855-1861.
[5] SHEMER H, LINDEN K G. Photolysis, oxidation and subsequent toxicity of a mixture of polycyclic aromatic hydrocarbons in natural waters[J]. Journal of Photochemistry and Photobiology A, 2007, 187: 186-195.
[6] BEKBOLET M, CMAR Z, KILIC M, et al. Photocatalytic oxidation of dinitronaphthalenes: theory and experiment[J]. Chemosphere, 2009, 75(8): 1008-1014.
[7] ZENG Y, HONG P K A, WAVREK D A. Integrated chemical-biological treatment of benzo[a]pyrene[J]. Environmental Science & Technology, 2000, 34: 854-862.
[8] EL-ALAWI Y. Measurement of short- and long-term toxicity of polycyclic aromatic hydrocarbons using luminescent bacteria Ecotoxicol[J]. Environmental Safety, 2002, 51: 12-21.
[9] KIM H H. Nonthermal plasma processing for air-pollution control: a historical review, current issues, and future prospects[J]. Plasma Processes and Polymers, 2004, 1: 91-110.
[10] DURME J V, DEWULF J, LEYS C, et al. Combining non-thermal plasma with heterogeneous catalysis in waste gas treatment: a review[J]. Applied Catalysis B: Environmental, 2008, 78(3/4): 324-333.
[11] CHEN H L, LEE H M, CHEN S H, et al. Removal of volatile organic compounds by single-stage and two-stage plasma catalysis systems: a review of the performance enhancement mechanisms, current status, and suitable applications[J]. Environmental Science & Technology, 2009, 43(7): 2216-2227.
[12] YE Z, ZHANG Y, LI P, et al. Feasibility of destruction of gaseous benzene with dielectric barrier discharge[J]. Journal of Hazardous Material, 2008, 90(1/2): 356-364.
[13] BLIN-SIMIAND N, JORAND F, MAGNE L,et al. Plasma reactivity and plasma-surface interactions during treatment of toluene by a dielectric barrier discharge[J]. Plasma Chemistry and Plasma Processing, 2008, 28(4): 429-466.
[14] KRAWEZYK K, ULEJCZYK B, SONG H K, et al. Plasma-catalytic reactor for decomposition of chlorinated hydrocarbons[J]. Plasma Chemistry and Plasma Processing, 2009, 29(1): 27-41.
[15] MOK Y S, DEMIDYUK V,WHITEHEAD J C. Decomposition of hydrofluorocarbons in a dielectric-packed plasma reactor[J]. Journal of Physical Chemistry A, 2008, 112(29): 6586-6591.
[16] OSTAPCZUK A, HAKODA T, SHIMADA A, et al. Naphthalene and acenaphthene decomposition by electron beam generated plasma application[J]. Plasma Chemistry and Plasma Processing, 2009, 28(4): 483-494.
[17] YU L, LI X, TU X, et al. Decomposition of naphthalene by dc gliding arc gas discharge[J]. Journal of Physical Chemistry A, 2010, 114(1): 360-368.
[18] ABDELAZIZ A A, SETO T, ABDEL-SALAM M, et al. Performance of a surface dielectric barrier discharge based reactor for destruction of naphthalene in an air stream[J]. Journal of Physics D: Applied Physics, 2012, 45(11): 110.
[19] HARLING A M, GLOVER D J, WHITEHEAD J C, et al. The role of ozone in the plasma-catalytic destruction of environmental pollutants[J]. Applied Catalysis B: Environmental, 2009, 90(1/2): 157-161.
[20] YU L, LI X D, TU X, et al. Decomposition of Naphthalene by dc Gliding Arc Gas Discharge[J]. Journal of Physical Chemistry A, 2010, 114: 360-368.
[21] SIMIAND N B, JORAND F, MAGNE L, et al. Plasma reactivity and plasma-surface interactions during treatment of toluene by a dielectric barrier discharge[J]. Plasma Chemistry and Plasma Processing, 2008, 28(4): 429-466.