Kinetic study of coals gasification into carbon dioxide atmosphere; MATEC Web of Conferences; Vol. 23 : Heat and Mass Transfer in the Thermal Control System of Technical and Technological Energy Equipment
| Parent link: | MATEC Web of Conferences Vol. 23 : Heat and Mass Transfer in the Thermal Control System of Technical and Technological Energy Equipment.— 2015.— [01020, 6 p.] |
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| סיכום: | Title screen The solid fuel gasification process was investigated to define chemical reactions rate and activation energy for a gas-generator designing and regime optimizing. An experimental procedure includes coal char samples of Kuznetskiy and Kansko-Achinskiy deposits consequent argon pyrolysis into argon and oxidating into carbon dioxide with different temperatures. The thermogravimetric analysis data of coal char gasification into carbon dioxide was obtained in the temperature range 900-1200°С. The mass loss and gasification time dependencies from temperature were defined to calculate chemical reaction frequency factor and activation energy. Two coal char gasification physico-mathematical models were proposed and recommendations for them were formed. |
| שפה: | אנגלית |
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2015
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| גישה מקוונת: | http://dx.doi.org/10.1051/matecconf/20152301020 http://earchive.tpu.ru/handle/11683/15370 |
| פורמט: | MixedMaterials אלקטרוני Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=645226 |
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| 200 | 1 | |a Kinetic study of coals gasification into carbon dioxide atmosphere |f A. G. Korotkikh, K. V. Slusarskiy (Slyusarsky) | |
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| 300 | |a Title screen | ||
| 320 | |a [References: 10 tit.] | ||
| 330 | |a The solid fuel gasification process was investigated to define chemical reactions rate and activation energy for a gas-generator designing and regime optimizing. An experimental procedure includes coal char samples of Kuznetskiy and Kansko-Achinskiy deposits consequent argon pyrolysis into argon and oxidating into carbon dioxide with different temperatures. The thermogravimetric analysis data of coal char gasification into carbon dioxide was obtained in the temperature range 900-1200°С. The mass loss and gasification time dependencies from temperature were defined to calculate chemical reaction frequency factor and activation energy. Two coal char gasification physico-mathematical models were proposed and recommendations for them were formed. | ||
| 461 | 0 | |0 (RuTPU)RU\TPU\network\4526 |t MATEC Web of Conferences | |
| 463 | 0 | |0 (RuTPU)RU\TPU\network\9794 |t Vol. 23 : Heat and Mass Transfer in the Thermal Control System of Technical and Technological Energy Equipment |o April 22-23, 2015, Tomsk, Russia |f National Research Tomsk Polytechnic University (TPU) ; ed. G. V. Kuznetsov [et al.] |o [proceedings] |v [01020, 6 p.] |d 2015 | |
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