Some laboratory experimental designs for obtaining dynamic property data on dioxins.
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[1] W M Shaub,et al. Dioxin formation in incinerators. , 1983, Environmental science & technology.
[2] D. T. Lynch,et al. On the separability of catalyst activity and kinetic behavior , 1989 .
[3] John H. Seinfeld,et al. Fundamentals of Air Pollution Engineering , 1988 .
[4] Stellan Marklund,et al. Correlation of incineration parameters for the destruction of polychlorinated dibenzo-p-dioxins , 1989 .
[5] S. Pratsinis. Simultaneous nucleation, condensation, and coagulation in aerosol reactors , 1988 .
[6] H. Hagenmaier,et al. Catalytic effects of fly ash from waste incineration facilities on the formation and decomposition of polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofurans , 1987 .
[7] M. Tysklind,et al. Emissions of PCDDs and PCDFs from a PVC-five in Holmsund, Sweden , 1989 .
[8] Charles N. Satterfield,et al. Mass transfer in heterogeneous catalysis , 1969 .
[9] Albert Merz,et al. Chemisch-verfahrenstechnische Aspekte zur Dioxinreduzierung bei Abfallverbrennungsprozessen , 1989 .
[10] F. Karasek,et al. Model studies of polychlorinated dibenzo-p-dioxin formation during municipal refuse incineration. , 1987, Science.
[11] James J. Carberry,et al. Chemical and catalytic reaction engineering , 1976 .
[12] F. Karasek,et al. Determination of Desorption Losses of Polychlorinated Dibenzo-p-Dioxins from Municipal Incinerator Flyash by Gas Chromatography/Mass Spectrometry , 1986 .
[13] H. Vogg,et al. Thermal behavior of PCDD/PCDF in fly ash from municipal incinerators , 1986 .
[14] B. Dellinger,et al. High-temperature gas-phase formation and destruction of polychlorinated dibenzofurans☆ , 1985 .
[15] A. Varma,et al. Catalytic reactions in transport-line reactors , 1979 .
[16] S. Uchida,et al. Reaction kinetics of formation of hydrochloric acid in municipal refuse incinerators , 1983 .
[17] P. Walker,et al. Detection of low temperature carbon gasification using DSC and TGA , 1989 .
[18] J. Pedersen,et al. Phenol and HCl at 550 °C yield a large variety of chlorinated toxic compounds , 1986, Nature.
[19] E. Ritter,et al. Chlorobenzene and Dichlorobenzene Reactions in Hydrogen and in Hydrogen/Oxygen Mixtures , 1990 .
[20] J. Falconer,et al. Temperature-Programmed Desorption and Reaction: Applications to Supported Catalysts , 1983 .
[21] T. Goldfarb. Evidence for post-furnace formation of PCDDs and PCDFs—Implications for control , 1989 .
[22] E. Christoffel. Laboratory Reactors and Heterogeneous Catalytic Processes , 1982 .
[23] S. Friedlander. The behavior of constant rate aerosol reactors , 1981 .
[24] J. Carberry. Structure sensitivity in heterogeneous catalysis: Activity and yield/selectivity , 1988 .
[25] T. Nestrick,et al. Thermolytic surface-reaction of benzene and iron (III) chloride to form chlorinated dibenzo-p-dioxins and dibenzofurans , 1987 .
[26] H. Bautz,et al. Carbonaceous particles in fly ash: a source for the de-novo-synthesis of organochlorocompounds , 1989 .
[27] S. Friedlander,et al. Aerosol reactor design: Effect of reactor geometry on powder production and vapor deposition , 1986 .
[28] Ravi K. Konduri,et al. Polychlorinated dioxin/furan formation in incinerators , 1990 .
[29] G. Eiceman,et al. Chlorination reactions of 1,2,3,4-tetrachlorodibenzo-p-dioxin on fly ash with HC1 in air , 1982 .
[30] S. S. Penner,et al. A simplified model for dioxin and furan formation in municipal-waste incinerators☆ , 1988 .
[31] J. Pedersen,et al. Formation of chlorinated organic compounds during combustion of propane in the presence of HCl , 1987 .
[32] J. Pedersen,et al. Methane, hydrogen chloride and oxygen form a wide range of chlorinated organic species in the temperature range 400°C–950°C☆ , 1988 .
[33] S. Senkan,et al. Chemical structures of fuel-rich, premixed, laminar flames of CH2Cl2 and CH4 , 1990 .