Physical-Mathematical Model for Fixed-Bed Solid Fuel Gasification Process Simulation; MATEC Web of Conferences; Vol. 91 : Smart Grids 2017
| Parent link: | MATEC Web of Conferences Vol. 91 : Smart Grids 2017.— 2017.— [01011, 5 p.] |
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| Egile nagusia: | |
| Erakunde egilea: | |
| Beste egile batzuk: | , |
| Gaia: | Title screen Phycial-mathmatical model for fixed-bed coal gasification process simulation is proposed. The heterogeneous carbon oxidation chemical reactions were simulated via Arrhenius equation while homogeneous reactions in gas phase were calculated using Gibbs free energy minimization procedure. The syngas component concentration field and fuel conversion distribution as well as syngas final temperature and composition were defined for fixed bed gasification of T-grade coal of Kuznetskiy deposit. The optimal fuel residence time and gasifyer specific productivity were defined. The prevail reactions in oxidizing and reduction zones together with its height were defined. |
| Hizkuntza: | ingelesa |
| Argitaratua: |
2017
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| Sarrera elektronikoa: | http://dx.doi.org/10.1051/matecconf/20179101011 http://earchive.tpu.ru/handle/11683/36599 |
| Formatua: | Baliabide elektronikoa Liburu kapitulua |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652887 |
| Gaia: | Title screen Phycial-mathmatical model for fixed-bed coal gasification process simulation is proposed. The heterogeneous carbon oxidation chemical reactions were simulated via Arrhenius equation while homogeneous reactions in gas phase were calculated using Gibbs free energy minimization procedure. The syngas component concentration field and fuel conversion distribution as well as syngas final temperature and composition were defined for fixed bed gasification of T-grade coal of Kuznetskiy deposit. The optimal fuel residence time and gasifyer specific productivity were defined. The prevail reactions in oxidizing and reduction zones together with its height were defined. |
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| DOI: | 10.1051/matecconf/20179101011 |