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Article

Development of a Chemical Quasi-Equilibrium Model of Biomass Waste Gasification in a Fluidized-Bed Reactor by Using Aspen Plus

1
Department of Agricultural and Forestry Sciences (DAFNE), Tuscia University of Viterbo, Via San Camillo de Lellis, 01100 Viterbo, Italy
2
Department of Nuclear, Subnuclear and Radiation Physics, Marconi University, 00193 Rome, Italy
*
Author to whom correspondence should be addressed.
Energies 2020, 13(1), 53; https://doi.org/10.3390/en13010053
Submission received: 5 November 2019 / Revised: 16 December 2019 / Accepted: 17 December 2019 / Published: 20 December 2019
(This article belongs to the Special Issue Hydrogen Production from Biomass)

Abstract

In the delicate context of climate change, biomass gasification has been demonstrated to be a very useful technology to produce power and hydrogen. Nevertheless, in literature, there is a lack of a flexible and fast but accurate model of biomass gasification that can be used with all the combinations of oxidizing agents, taking into account both organic and inorganic contaminants, and able to give results that are more realistic. In order to do that, a model of biomass gasification has been developed using the chemical engineering software Aspen Plus. The developed model is based on the Gibbs free energy minimization applying the restricted quasi-equilibrium approach via Data-Fit regression from experimental data. The simulation results obtained, considering different mixes of gasifying agents, were compared and validated against experimental data reported in literature for the most advanced fluidized bed technology. The maximum discrepancy value obtained for hydrogen, with respect to experimental data, is of 8%, and all the other values reached by the developed simulations, considering both organic and inorganic compounds, are in good agreement with literature data. The gas yield reached by the developed simulation is in the range of 1.1–1.3 Nm3/kg.
Keywords: biomass gasification; equilibrium model; tar; syngas; hazelnut shells; Gibbs free energy minimization; steam gasification; Aspen Plus biomass gasification; equilibrium model; tar; syngas; hazelnut shells; Gibbs free energy minimization; steam gasification; Aspen Plus

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MDPI and ACS Style

Marcantonio, V.; Bocci, E.; Monarca, D. Development of a Chemical Quasi-Equilibrium Model of Biomass Waste Gasification in a Fluidized-Bed Reactor by Using Aspen Plus. Energies 2020, 13, 53. https://doi.org/10.3390/en13010053

AMA Style

Marcantonio V, Bocci E, Monarca D. Development of a Chemical Quasi-Equilibrium Model of Biomass Waste Gasification in a Fluidized-Bed Reactor by Using Aspen Plus. Energies. 2020; 13(1):53. https://doi.org/10.3390/en13010053

Chicago/Turabian Style

Marcantonio, Vera, Enrico Bocci, and Danilo Monarca. 2020. "Development of a Chemical Quasi-Equilibrium Model of Biomass Waste Gasification in a Fluidized-Bed Reactor by Using Aspen Plus" Energies 13, no. 1: 53. https://doi.org/10.3390/en13010053

APA Style

Marcantonio, V., Bocci, E., & Monarca, D. (2020). Development of a Chemical Quasi-Equilibrium Model of Biomass Waste Gasification in a Fluidized-Bed Reactor by Using Aspen Plus. Energies, 13(1), 53. https://doi.org/10.3390/en13010053

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