Kinetic Modeling and Optimization of Biomass Gasification in Bubbling Fluidized Bed Gasifier Using Response Surface Method
نویسندگان
چکیده
This paper presents the kinetic modeling of biomass gasification in bubbling fluidized bed (BFB) gasifiers and optimization methods to maximize products. The model was developed based on two-phase fluidization theory. In this work, reaction kinetics, hydrodynamic conditions, convective diffusion effect, thermal cracking tar kinetics were considered model. coded MATLAB simulated. result depicted good agreement with experimental work literature. sensitivity analysis carried out effect temperature ranging from 650 850 steam ratio (S/B) 0.1 2 investigated. showed that an increase promoted H2 production 18.73 % 36.87 %, reduced CO 39.97 34.2 CH4 18.01 11.65 %. Furthermore, surface response constructed regression mutual S/B products heating value addition, desirability function employed optimize product value. maximum yield obtained at 827.9 S/B. predicted by these optimum operational conditions 30.1 44.1 13.2 12.9 14.035 MJ/Nm3, 14.5 MJ/Nm3 for H2, CO, CO2, CH4, LHV, HHV, respectively. Kinetic BFB process is still under development, which considers cracking, behavior. Moreover, large number previous studies gave priority a single parameter investigation. However, investigation can be extended various parameters simultaneously, would give solid information system performance analysis.
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ژورنال
عنوان ژورنال: International Journal of Renewable Energy Development
سال: 2022
ISSN: ['2252-4940']
DOI: https://doi.org/10.14710/ijred.2022.45179