参考文献

[1]Sean,M H,Aylward L L.Dioxin risks in perspective:past,present,and future[J].Regulatory Toxicology and Pharmacology,2003(37):202-217.

[2]McKay G.Dioxin characterisation,formation and minimisation during municipal solid waste(MSW)incineration:review[J].Chemical Engineering Journal,2002,86(3):343-368.

[3]盖虹云,全翔翼.二英的毒性及其对人体健康的影响[J].包头医学院学报,2002,18(4):370-372.

[4]孙成均.二英类化合物的环境污染,毒性及分析方法[J].现代预防医学,2000,27(1):63-66.

[5]苏国臣,张金波,苏晶林.环境中的二英及其对人体的危害[J].国外医学卫生学分册,2003,30(1):13-16.

[6]Kulkarni P S,Crespo J G,Afonso C A M.Dioxins sources and current remediation technologies—A review[J]. Environment International,2008,34(1):139-153.

[7]Weber R,Sakurai T,Hagenmaier H.Low temperature decomposition of PCDD/PCDF,chlorobenzenes and PAHs by TiO2-basedV2O5-WO3catalysts[J].Applied Catalysis B:Environmental,1999,20(4):249-256.

[8]Krishnamoorthy S,Rivas J A,Amiridis M D.Catalytic Oxidation of 1,2-Dichlorobenzene over Supported Transition Metal Oxides[J].Journal of Catalysis,2000,193(2):264-272.

[9]Poplawski K,Lichtenberger J,Frerich J K,et al.Catalytic oxidation of 1,2-dichlorobenzene over ABO3-type perovskites[J].Catalysis Today,2000,62(4):329-336.

[10]吴西宁,田洪海,庞菊玲等.催化氧化脱除垃圾焚烧烟气中二英类的研究[J].工业催化,2004,12(9):47-50.

[11]韦平英,侯美珍,莫德清等.环境中二英及其控制、降解技术[J].环境科学动态,2002(2):34-36.

[12]谭茜,许佩瑶.二英催化分解技术研究进展[J].环境与可持续发展,2007(2):18-20.

[13]郑小萍.环境空气中VOCs的监测技术新进展[J].环境监测管理与技术,2001(3):15-17.

[14]刘鹏,周湘梅.VOC的回收与处理技术简介[J].石油化工环境保护,2001(3):39-42.

[15]李婕,羌宁.挥发性有机物(VOCs)活性炭吸附回收技术综述[J].四川环境,2007(6):101-105,111.

[16]薛勇江,俞雪燕,田桂芝.室内空气中挥发性有机化合物(VOCs)检测技术的改进[J].化学工程师,2006(5):30-31,33.

[17]黄正宏,康飞宇,杨骏兵等.活性炭纤维对挥发性有机物的吸附及其等温线的拟合[J].离子交换与吸附,2001(6):487-493.

[18]周玉昆.挥发性有机化合物的污染控制技术[J].化工环保,1993(4):199-202.

[19]闫勇.有机废气中VOC的回收方法[J].化工环保,1997(6):332-335.

[20]王志伟,耿春香,安慧.膜法回收有机蒸汽进展[J].环境科学与管理,2009(3):100-105.

[21]闫勇.有机废气中挥发性有机物(VOC)的净化回收技术-炭吸附和膜分离[J].化工进展,1996(5):26-28,40.

[22]魏东洋,刘芬,许振成等.降解氯苯类化合物研究进展[J].安徽农业科学,2009(32):15681-15683.

[23]唐伟.钙钛矿型催化剂对VOCs催化燃烧的研究[M].浙江:浙江工业大学,2005.

[24]Lomnicki S,Lichtenberger J,Xu Z T,et al.Catalytic oxidation of 2,4,6-trichlorophenol overVanadia/titania-based catalysts[J].Applied Catalysis B:Environmental,2003,46(1):105-119.

[25]Lomnicki S,Dellinger B.Formation of PCDD/F from the pyrolysis of 2-chlorophenol on the surface of dispersed copper oxide particles[J].Proceedings of the Combustion Institute,2002,29(2):2463-2468.

[26]Finocchio E,Baldi M,Busca G,et al.A study of the abatement ofVOC overV2O5-WO3-TiO2and alternative SCR catalysts[J].Catalysis Today,2000,59(3-4):261-268.

[27]Chang M B,Chi K H,Chang-Chien G P.Evaluation of PCDD/F congener distributions in MWI flue gas treated with SCR catalysts[J].Chemosphere,2004,55(11):1457-1467.

[28]何毅,王华,李光明等.有机废气催化燃烧技术[J].江苏环境科技,2004,17(1):35-38.

[29]向辉.催化燃烧气相二英类污染物的研究[D].长沙:中南大学[J].2011.

[30]张玉海.二英类物质去除降解研究[D].华北电力大学,2007.

[31]Yang C C,Chang S H,Hong B Z,et al.Innovative PCDD/F-containing gas stream generating system applied in catalytic decomposition of gaseous dioxins overV2O5-WO3/TiO2-based catalysts[J].Chemosphere,2008,73(6):890-895.

[32]Lomnicki S,Lichtenberger J,Xu Z,et al.Catalytic oxidation of 2,4,6-trichlorophenol overVanadia/titania-based catalysts[J].Applied Catalysis B:Environmental,2003,46(1):105-119.

[33]Krishnamoorthy S,Rivas J A,Amiridis M D.Catalytic Oxidation of 1,2-Dichlorobenzene over Supported Transition Metal Oxides[J].Journal of Catalysis,2000,193(2):264-272.

[34]Weber R,Plinke M,Xu Z,et al.Destruction efficiency of catalytic filters for polychlorinated dibenzo-p-dioxin and dibenzofurans in laboratory test and field operation-insight into destruction and adsorption behavior of semivolatile compounds[J].Applied Catalysis B:Environmental,2001,31(3):195-207.

[35]Debecker D P,Bouchmella K,Delaigle R,et al.One-step non-hydrolytic sol-gel preparation of efficientV2O5-TiO2catalysts forVOC total oxidation[J].Applied Catalysis B:Environmental,2010,94(1-2):38-45.

[36]Keller D E,Koningsberger D C,Weckhuysen B M.Elucidation of the molecular structure of hydratedVanadium oxide species by X-ray absorption spectroscopy:correlation between theV-V coordination number and distance and the point of zero charge of the support oxide[J].Physical Chemistry Chemical Physics,2006,8(41):4814-4824.

[37]Bertinchamps F,Gregoire C,Gaigneaux E M.Systematic investigation of supported transition metal oxide based formulations for the catalytic oxidative elimination of(chloro)-aromatics:Part I:Identification of the optimal main active phases and supports[J].Applied Catalysis B:Environmental,2006,66(1-2):1-9.

[38]Leyrer J,Margraf R,Taglauer E,et al.Solid-solid wetting and formation of monolayers in supported oxide systems[J].Surface Science,1988,201(3):603-623.

[39]Bertinchamps F,Grégoire C,Gaigneaux E M.Systematic investigation of supported transition metal oxide based formulations for the catalytic oxidative elimination of(chloro)-aromatics:Part II:Influence of the nature and addition protocol of secondary phases toVOx/TiO2[J].Applied Catalysis B:Environmental,2006,66(1-2):10-22.

[40]Ferreira M L,Volpe M.A combined theoretical and experimental study of supportedVanadium oxide catalysts[J]. Journal of Molecular Catalysis A:Chemical,2002,184(1-2):349-360.

[41]Albonetti S,Blasioli S,Bonelli R,et al.The role of acidity in the decomposition of 1,2-dichlorobenzene over TiO2-basedV2O5/WO3catalysts[J].Applied Catalysis A:General,2008,341(1-2):18-25.

[42]Debecker D P,Delaigle R,Bouchmella K,et al.Total oxidation of benzene and chlorobenzene with MoO3-and WO3-promotedV2O5/TiO2catalysts prepared by a nonhydrolytic sol-gel route[J].Catalysis Today,2010,157(1-4):125-130.

[43]Djerad S,Tifouti L,Crocoll M,et al.Effect ofVanadia and tungsten loadings on the physical and chemical characteristics ofV2O5-WO3/TiO2catalysts[J].Journal of Molecular Catalysis A:Chemical,2004,208(1-2):257-265.

[44]万总.降解气相二英污染物催化剂的成型与应用研究[D].长沙:中南大学[J].2011.