Non-isothermal kinetic study of bituminous coal and lignite conversion in air and in argon/air mixtures / K. V. Slusarskiy (Slyusarsky) [et al.]

Уровень набора: FuelАльтернативный автор-лицо: Slusarskiy (Slyusarsky), K. V., specialist in the field of power engineering, assistant of Tomsk Polytechnic University, 1990-, Konstantin Vitalievich;Larionov, K. B., specialist in the field of power engineering, technician of Tomsk Polytechnic University, 1990-, Kirill Borisovich;Osipov, V. I., Vitaly Igorevich;Yankovsky, S. A., specialist in the field of power engineering, engineer of Tomsk Polytechnic University, assistant, 1985-, Stanislav Aleksandrovich;Gubin, V. E., specialist in the field of power engineering, Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences, 1976-, Vladimir Evgenievich;Gromov, A. A., Aleksandr AleksandrovichКоллективный автор (вторичный): Национальный исследовательский Томский политехнический университет, Инженерная школа энергетики, Научно-образовательный центр И. Н. Бутакова (НОЦ И. Н. Бутакова)Язык: английский.Резюме или реферат: The exact characteristics of the pyrolysis and combustion kinetics for Siberian bituminous coals and lignites were studied for better understanding of the fuel conversion processes. The bituminous coal samples of Kuznetskiy deposit and lignite samples of Kansko-Achinsk deposit were investigated in argon and in argon/air gas mixtures. The pyrolysis and oxidation experiments were executed at four heating rates (5, 10, 20 and 30 °C/min) under TG/DSC analyses coupled with mass-spectrometry. The activation energy for bituminous coal and lignite samples was decreased with conversion degree during oxidation. The combustion products of highest oxidation degree (CO2 and H2O) were dominated in gases released in oxidizing atmosphere. Contrariwise, activation energy was increased during pyrolysis with high content of CO, CO2, H2O, CH4, and H2 in released gases.The two isoconversional models were applied to determine the activation energy dependence on fuel samples conversion: Starink model and Ozawa iterative procedure. The mean arithmetic values of the resulted activation energy were 60 kJ/mole and 400 kJ/mole for oxidation and pyrolysis processes, respectively. These values are in good agreement with the results, presented previously for the other coals. The Starink model showed higher accuracy and lower activation energy values. The heating rate by non-isothermal oxidation and pyrolysis had the significant influence on the reaction rate because of evolution processes of the reactive surface and pore structure of the coal samples..Примечания о наличии в документе библиографии/указателя: [References: p. 392 (32 tit.)].Аудитория: .Тематика: электронный ресурс | труды учёных ТПУ | неизотермические процессы | кинетика | энергия активации | термогравиметрия | угольные месторождения Ресурсы он-лайн:Щелкните здесь для доступа в онлайн
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[References: p. 392 (32 tit.)]

The exact characteristics of the pyrolysis and combustion kinetics for Siberian bituminous coals and lignites were studied for better understanding of the fuel conversion processes. The bituminous coal samples of Kuznetskiy deposit and lignite samples of Kansko-Achinsk deposit were investigated in argon and in argon/air gas mixtures. The pyrolysis and oxidation experiments were executed at four heating rates (5, 10, 20 and 30 °C/min) under TG/DSC analyses coupled with mass-spectrometry. The activation energy for bituminous coal and lignite samples was decreased with conversion degree during oxidation. The combustion products of highest oxidation degree (CO2 and H2O) were dominated in gases released in oxidizing atmosphere. Contrariwise, activation energy was increased during pyrolysis with high content of CO, CO2, H2O, CH4, and H2 in released gases.The two isoconversional models were applied to determine the activation energy dependence on fuel samples conversion: Starink model and Ozawa iterative procedure. The mean arithmetic values of the resulted activation energy were 60 kJ/mole and 400 kJ/mole for oxidation and pyrolysis processes, respectively. These values are in good agreement with the results, presented previously for the other coals. The Starink model showed higher accuracy and lower activation energy values. The heating rate by non-isothermal oxidation and pyrolysis had the significant influence on the reaction rate because of evolution processes of the reactive surface and pore structure of the coal samples.

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