A new model for coal gasification on pressurized bubbling fluidized bed gasifiers

Cristian Sánchez, Erika Arenas, Farid Chejne, Carlos A. Londoño, Sebastian Cisneros, Juan C. Quintana

    Resultado de la investigación: Contribución a una revistaArtículorevisión exhaustiva

    29 Citas (Scopus)

    Resumen

    Many industries have taken interest in the use of coal gasification for the production of chemicals and fuels. This gasification can be carried out inside a fluidized bed reactor. This non-ideal reactor is difficult to predict due to the complex physical phenomena and the different chemical changes that the feedstock undergoes. The lack of a good model to simulate the reactor's behavior produces less efficient processes and plant designs. Various approaches to the proper simulation of such reactor have been proposed. In this paper, a new model is developed for the simulation of a pressurized bubbling fluidized bed (PBFB) gasifier that rigorously models the physical phenomena and the chemical changes of the feedstock inside the reactor. In the model, the reactor is divided into three sections; devolatilization, volatile reactions and combustion-gasification. The simulation is validated against experimental data reported in the literature and compared with other models proposed by different authors; once the model is validated, the dependence of the syngas composition on operational pressure, temperature, steam/coal and air/coal ratios are studied. The results of this article show how this model satisfactorily predicts the performance of PBFB gasifiers.

    Idioma originalInglés
    Páginas (desde-hasta)717-723
    Número de páginas7
    PublicaciónEnergy Conversion and Management
    Volumen126
    DOI
    EstadoPublicada - 15 oct. 2016

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    © 2016 Elsevier Ltd

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