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Simulation of Steam Gasification in a Fluidized Bed Reactor with Energy Self-Sufficient Condition

Author

Listed:
  • Ajaree Suwatthikul

    (Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand)

  • Siripong Limprachaya

    (Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand)

  • Paisan Kittisupakorn

    (Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand)

  • Iqbal Mohammed Mujtaba

    (School of Engineering, University of Bradford, Bradford BD7 1DP, UK)

Abstract

The biomass gasification process is widely accepted as a popular technology to produce fuel for the application in gas turbines and Organic Rankine Cycle (ORC). Chemical reactions of this process can be separated into three reaction zones: pyrolysis, combustion, and reduction. In this study, sensitivity analysis with respect to three input parameters (gasification temperature, equivalence ratio, and steam-to-biomass ratio) has been carried out to achieve energy self-sufficient conditions in a steam gasification process under the criteria that the carbon conversion efficiency must be more than 70%, and carbon dioxide gas is lower than 20%. Simulation models of the steam gasification process have been carried out by ASPEN Plus and validated with both experimental data and simulation results from Nikoo & Mahinpey (2008). Gasification temperature of 911 °C, equivalence ratio of 0.18, and a steam-to-biomass ratio of 1.78, are considered as an optimal operation point to achieve energy self-sufficient condition. This operating point gives the maximum of carbon conversion efficiency at 91.03%, and carbon dioxide gas at 15.18 volumetric percentages. In this study, life cycle assessment (LCA) is included to compare the environmental performance of conventional and energy self-sufficient gasification for steam biomass gasification.

Suggested Citation

  • Ajaree Suwatthikul & Siripong Limprachaya & Paisan Kittisupakorn & Iqbal Mohammed Mujtaba, 2017. "Simulation of Steam Gasification in a Fluidized Bed Reactor with Energy Self-Sufficient Condition," Energies, MDPI, vol. 10(3), pages 1-15, March.
    • Handle: RePEc:gam:jeners:v:10:y:2017:i:3:p:314-:d:92245
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    References listed on IDEAS

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    Cited by:

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    2. Sara Rajabi Hamedani & Mauro Villarini & Andrea Colantoni & Michele Moretti & Enrico Bocci, 2018. "Life Cycle Performance of Hydrogen Production via Agro-Industrial Residue Gasification—A Small Scale Power Plant Study," Energies, MDPI, vol. 11(3), pages 1-19, March.
    3. María Pilar González-Vázquez & Fernando Rubiera & Covadonga Pevida & Daniel T. Pio & Luís A.C. Tarelho, 2021. "Thermodynamic Analysis of Biomass Gasification Using Aspen Plus: Comparison of Stoichiometric and Non-Stoichiometric Models," Energies, MDPI, vol. 14(1), pages 1-17, January.
    4. Aghaalikhani, Arash & Schmid, Johannes C. & Borello, Domenico & Fuchs, Joseph & Benedikt, Florian & Hofbauer, Herman & Rispoli, Franco & Henriksen, Ulrick B. & Sárossy, Zsuzsa & Cedola, Luca, 2019. "Detailed modelling of biomass steam gasification in a dual fluidized bed gasifier with temperature variation," Renewable Energy, Elsevier, vol. 143(C), pages 703-718.
    5. Qitai Eri & Wenzhen Wu & Xinjun Zhao, 2017. "Numerical Investigation of the Air-Steam Biomass Gasification Process Based on Thermodynamic Equilibrium Model," Energies, MDPI, vol. 10(12), pages 1-19, December.
    6. M. Shahabuddin & Sankar Bhattacharya, 2021. "Co-Gasification Characteristics of Coal and Biomass Using CO 2 Reactant under Thermodynamic Equilibrium Modelling," Energies, MDPI, vol. 14(21), pages 1-12, November.

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