Effect of CO2 temperature and particle size distribution of fuel on the gasification kinetic parameters; 11th International Forum on Strategic Technology (IFOST 2016); Pt. 2
| Parent link: | 11th International Forum on Strategic Technology (IFOST 2016): 1-3 June 2016, Novosibirsk, Russiain/ Novosibirsk State Technical University.— , 2016 Pt. 2.— 2016.— [P. 580-583] |
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| Streszczenie: | Title screen The three coal char samples gasification processes at various temperature in carbon dioxide were studied via thermogravimetry analyzer Netzsch STA 449. Samples of Kuznetskiy deposit anthracite and bituminous coal and Kansko-Achinskiy deposit lignite with different carbon content were used. Experimental results were analyzed via three kinetic models: volumetric, shrinking core and random pore. The particle size distribution function was used as well. The obtained activation energy values are in good agreement with previously published data. The particle size distribution function implementation in reaction rate analysis allowed to increase a correlation coefficient value up to 0,9 for all models. Режим доступа: по договору с организацией-держателем ресурса |
| Język: | angielski |
| Wydane: |
2016
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| Seria: | Applied engineering |
| Hasła przedmiotowe: | |
| Dostęp online: | http://dx.doi.org/10.1109/IFOST.2016.7884327 |
| Format: | Elektroniczne Rozdział |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654609 |
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| 200 | 1 | |a Effect of CO2 temperature and particle size distribution of fuel on the gasification kinetic parameters |f A. G. Korotkikh, K. V. Slusarskiy (Slyusarsky) | |
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| 225 | 1 | |a Applied engineering | |
| 300 | |a Title screen | ||
| 320 | |a [References: p. 583 (8 tit.)] | ||
| 330 | |a The three coal char samples gasification processes at various temperature in carbon dioxide were studied via thermogravimetry analyzer Netzsch STA 449. Samples of Kuznetskiy deposit anthracite and bituminous coal and Kansko-Achinskiy deposit lignite with different carbon content were used. Experimental results were analyzed via three kinetic models: volumetric, shrinking core and random pore. The particle size distribution function was used as well. The obtained activation energy values are in good agreement with previously published data. The particle size distribution function implementation in reaction rate analysis allowed to increase a correlation coefficient value up to 0,9 for all models. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | 1 | |0 (RuTPU)RU\TPU\network\20157 |t 11th International Forum on Strategic Technology (IFOST 2016) |o 1-3 June 2016, Novosibirsk, Russiain |o in 2 pt. |o [proceedings] |f Novosibirsk State Technical University |d 2016 | |
| 463 | 0 | |0 (RuTPU)RU\TPU\network\20159 |t Pt. 2 |v [P. 580-583] |d 2016 | |
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a gasification | |
| 610 | 1 | |a coal | |
| 610 | 1 | |a particle size | |
| 610 | 1 | |a thermogravimetry | |
| 610 | 1 | |a kinetic model | |
| 610 | 1 | |a activation energy | |
| 610 | 1 | |a carbon dioxide | |
| 610 | 1 | |a temperature | |
| 610 | 1 | |a газификация | |
| 610 | 1 | |a угли | |
| 610 | 1 | |a частицы | |
| 610 | 1 | |a термогравиметрия | |
| 610 | 1 | |a кинетические модели | |
| 610 | 1 | |a размеры | |
| 610 | 1 | |a энергия активации | |
| 610 | 1 | |a углекислый газ | |
| 610 | 1 | |a температура | |
| 700 | 1 | |a Korotkikh |b A. G. |c specialist in the field of power engineering |c Professor of Tomsk Polytechnic University, Doctor of Physical and Mathematical Sciences |f 1976- |g Aleksandr Gennadievich |3 (RuTPU)RU\TPU\pers\34763 |9 18113 | |
| 701 | 1 | |a Slusarskiy (Slyusarsky) |b K. V. |g Konstantin Vitalievich |f 1990- |c specialist in the field of power engineering |c Associate Professor of Tomsk Polytechnic University, Candidate of Physical and Mathematical Sciences |y Tomsk |3 (RuTPU)RU\TPU\pers\35634 |9 18803 | |
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