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Ozone synthesis under barrier discharge at high and low concentrations

Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The influence of discharge parameters on the obtained ozone concentration has been analysed by means of a simple model of synthesis under silent discharge conditions. The overall rate of ozone synthesis decreases with an increase in the ozone concentration. The maximum content of ozone is obtained when in specified conditions the rate of the reaction, in which ozone is formed will be equal with that of the reactions causing its decomposition. It has been found that for the model assumed, the temperature is the main parameter which influences the maximum ozone concentrations. The calculation models are often simplified, with omitting the endothermic effect of the ozone synthesis and without taking into account the rise in average molar specific heat of a gas mixture resulting from the presence of ozone in it besides oxygen. Calculations taking into account and then omitting the above parameters were carried out. It appears that their influence is insignificant, so the simplification of the model does not cause a significant error. This especially refers to the synthesis at low concentrations of ozone. Many times it has been experimentally found that at low ozone concentrations the better process efficiency, i.e. a little higher ozone concentration is obtained when the synthesis proceeds at a higher temperature (with maintaining the other experiment conditions invariable). This anomaly has been explained on the basis of experimental results and calculations using a simple model of the process. model of synthesis under silent discharge conditions. The overall rate of ozone synthesis decreases with an increase in the ozone concentration. The maximum content of ozone is obtained when in specified conditions the rate of the reaction, in which ozone is formed will be equal with that of the reactions causing its decomposition. It has been found that for the model assumed, the temperature is the main parameter which influences the maximum ozone concentrations. The calculation models are often simplified, with omitting the endothermic effect of the ozone synthesis and without taking into account the rise in average molar specific heat of a gas mixture resulting from the presence of ozone in it besides oxygen. Calculations taking into account and then omitting the above parameters were carried out. It appears that their influence is insignificant, so the simplification of the model does not cause a significant error. This especially refers to the synthesis at low concentrations of ozone. Many times it has been experimentally found that at low ozone concentrations the better process efficiency, i.e. a little higher ozone concentration is obtained when the synthesis proceeds at a higher temperature (with maintaining the other experiment conditions invariable). This anomaly has been explained on the basis of experimental results and calculations using a simple model of the process.
Rocznik
Strony
28--32
Opis fizyczny
Bibliogr. 18 poz., rys., tab.
Twórcy
autor
  • Warsaw University of Technology, Faculty of Chemistry, fax: (+22) 628-27-41
autor
  • Warsaw University of Technology, Faculty of Chemistry, fax: (+22) 628-27-41
autor
  • Warsaw University of Technology, Faculty of Chemistry, fax: (+22) 628-27-41
Bibliografia
  • (1) Rice, R. P., Ozone in the United States of America - state-of-the art, Ozone Sci. & Eng., 1999, 21, 99.
  • (2) Pollo, I., Remarks on the Research and the Application of Ozone in Poland, Ozone Sci. & Eng., 1999, 21, 177.
  • (3) Schmidt-Szałowski, K., Industrial ozone synthesis under electric discharge conditions (in Polish), Przem. Chem., 2000, 79, 115.
  • (4) Ozonek J, Fijałkowski S., Pollo I., A new approach to energy distribution in industrial ozonizers, Int. Ozone Symp. "Application of ozone in water and waste treatment". Warszawa, 1994, 218.
  • (5) Ozonek J., Pollo 1., Contribution of the problem of energy distribution in the process of ozone generation, 11th Int. Symp. On Plasma Chemistry, Loughborrough, 1993, vol. 2, 645.
  • (6) Ozonek J., Pollo I., Analysis of energy distribution in an ozonizer, Hakone 5, Milovy 1996, 31.
  • (7) Eliasson, B., Electical Discharge in Oxygen, Part 1, Brown Boveri Research Report No. KER 83-40 C, 1983.
  • (8) Samoilovich, V.C., Gibalov, V.l., Fiziczieskaja Chimija Bariernogo Razriada, Moskva, 1989.
  • (9) Eliasson, B., Kogelschatz, U., Strasser, S., Hirth, M., Electrical Discharge in Oxygen, Part 2, Brown Boveri Research Report No. KER 83-28 C, 1983.
  • (10) Petryk, J., Schmidt-Szałowski, K., Kinetic Model of Ozone Synthesis in Silent Discharges, Pol. J. Appl. Chem., 1998, 42, 105.
  • (11) Filippov, l.V., Vendillo, V.P., Elektriczeskaia teoria ozonatorov, Zh. Fiz. Chim., 1959, 33 (10), 2358.
  • (12) Kogelschatz, U., Process Technologies for Water Treatment, S. Stucki (Editor), Plenum Press, New York, London, 1988, 87.
  • (13) Braun, D., Kuehler, U., Pietsch, G, Mierodiseharges in Air-Fed Ozonizers, J. Phys. D: Appl. Phys., 1991, 24, 564.
  • (14) Murata, T., Tatsukawa, M., Okita, Y, Yasuoka, K., Polarity effect of silent discharge. Proc. 12th Ozone World Congress, Lille 1995, Yol. 2, 59.
  • (15) Drzimal, J., Gibalov, V. L, Samoilowitch, V. G, Struktura bariernogo razriada. Charakteristiki mikrorazriada, Zh. Fiz. Chim., 1988, 62, 3048.
  • (16) Rosoeha, L. A., Anderson, G. K., Beehtold, L. A., Coogan, J. J. et al., Non-Thermal Plasma Techniques for Pollution Control, Part B, Penetrante, B.M., Schultheis, S.E. (Editors), Springer Yerlag, Berlin Heidelberg 1993, 281.
  • (17) Jodzis, S., Petryk, J., Schmidt-Szałowski, K., Kinetic-Energetic Characteristics of Ozone Synthesis in an Ozonizer with Thermally Stabilised Electrodes, Proc. 14th ISPC, Praha 1999, 2307.
  • (18) Jodzis, S., Kowalczyk, S., Macrokinetics of the ozone synthesis process in silent discharges conditions. Proc. 15th ISPC, Orlean 2001, 2861.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS3-0002-0031
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