Kinetic modeling of biomass gasification in a micro fluidized bed

Wei Gao; Mohammad Reza Farahani; Mehdi Rezaei; Abdul Qudair Baig; Muhammad Kamran Jamil; Muhammad Imran; Reza Rezaee-Manesh

doi:10.1080/15567036.2016.1236302

Kinetic modeling of biomass gasification in a micro fluidized bed

Wei Gao, Mohammad Reza Farahani, Mehdi Rezaei, Abdul Qudair Baig, Muhammad Kamran Jamil, Muhammad Imran, Reza Rezaee-Manesh

Department of Mathematical Sciences

Research output: Contribution to journal › Article › peer-review

5 Citations (Scopus)

Abstract

This paper presents a goal programming model to predict the kinetic parameters of micro fluidized bed (Micro-FB) gasification of woody biomass in Qom, Iran. Qom has an abundance of waste woody biomass, and gasification can convert this residue into clean syngas. To do this, a kinetic model of biomass gasification was developed and validated against the experimental data available in the literature. The experiments were carried out in a Micro-FB in the presence of silica sand as the fluidization medium. To fully decompose the aromatic tars, the reaction temperatures were considered between 700°C and 1000°C with 100°C intervals. Results showed that the obtained activation energies strongly depend on the particle size for all the tested conditions.

Original language	English
Pages (from-to)	643-648
Number of pages	6
Journal	Energy Sources, Part A: Recovery, Utilization and Environmental Effects
Volume	39
Issue number	7
DOIs	https://doi.org/10.1080/15567036.2016.1236302
Publication status	Published - Apr 3 2017

Keywords

Micro-FB
fluidization
gasification
model
woody biomass

ASJC Scopus subject areas

Renewable Energy, Sustainability and the Environment
Nuclear Energy and Engineering
Fuel Technology
Energy Engineering and Power Technology

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10.1080/15567036.2016.1236302

Cite this

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title = "Kinetic modeling of biomass gasification in a micro fluidized bed",

abstract = "This paper presents a goal programming model to predict the kinetic parameters of micro fluidized bed (Micro-FB) gasification of woody biomass in Qom, Iran. Qom has an abundance of waste woody biomass, and gasification can convert this residue into clean syngas. To do this, a kinetic model of biomass gasification was developed and validated against the experimental data available in the literature. The experiments were carried out in a Micro-FB in the presence of silica sand as the fluidization medium. To fully decompose the aromatic tars, the reaction temperatures were considered between 700°C and 1000°C with 100°C intervals. Results showed that the obtained activation energies strongly depend on the particle size for all the tested conditions.",

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AU - Gao, Wei

AU - Farahani, Mohammad Reza

AU - Rezaei, Mehdi

AU - Qudair Baig, Abdul

AU - Jamil, Muhammad Kamran

AU - Imran, Muhammad

AU - Rezaee-Manesh, Reza

PY - 2017/4/3

Y1 - 2017/4/3

N2 - This paper presents a goal programming model to predict the kinetic parameters of micro fluidized bed (Micro-FB) gasification of woody biomass in Qom, Iran. Qom has an abundance of waste woody biomass, and gasification can convert this residue into clean syngas. To do this, a kinetic model of biomass gasification was developed and validated against the experimental data available in the literature. The experiments were carried out in a Micro-FB in the presence of silica sand as the fluidization medium. To fully decompose the aromatic tars, the reaction temperatures were considered between 700°C and 1000°C with 100°C intervals. Results showed that the obtained activation energies strongly depend on the particle size for all the tested conditions.

AB - This paper presents a goal programming model to predict the kinetic parameters of micro fluidized bed (Micro-FB) gasification of woody biomass in Qom, Iran. Qom has an abundance of waste woody biomass, and gasification can convert this residue into clean syngas. To do this, a kinetic model of biomass gasification was developed and validated against the experimental data available in the literature. The experiments were carried out in a Micro-FB in the presence of silica sand as the fluidization medium. To fully decompose the aromatic tars, the reaction temperatures were considered between 700°C and 1000°C with 100°C intervals. Results showed that the obtained activation energies strongly depend on the particle size for all the tested conditions.

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Kinetic modeling of biomass gasification in a micro fluidized bed

Abstract

Keywords

ASJC Scopus subject areas

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