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Energy and Exergy Analysis of High Temperature Agent Gasification of Biomass

Author

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  • Yueshi Wu

    (Division of Energy and Furnace Technology, Department of Material Science and Engineering, School of Industrial Engineering and Management, KTH-Royal Institute of Technology, Brinellvägen 23, 10044 Stockholm, Sweden)

  • Weihong Yang

    (Division of Energy and Furnace Technology, Department of Material Science and Engineering, School of Industrial Engineering and Management, KTH-Royal Institute of Technology, Brinellvägen 23, 10044 Stockholm, Sweden)

  • Wlodzimierz Blasiak

    (Division of Energy and Furnace Technology, Department of Material Science and Engineering, School of Industrial Engineering and Management, KTH-Royal Institute of Technology, Brinellvägen 23, 10044 Stockholm, Sweden)

Abstract

A chemical equilibrium model was developed to predict the product composition of a biomass gasification system using highly preheated air and steam. The advantages and limitations of this system were discussed from a thermodynamic viewpoint. The first and second law analyses have been conducted for various preheating temperatures and steam/biomass mass (S/B) ratios. The results demonstrated that the chemical energy output of the produced syngas is highest when the S/B ratio is 1.83 under the conditions used in this study. However, higher S/B ratios have a negative effect on the energy and exergy efficiencies. Higher preheating temperatures increase the chemical energy of the produced syngas and the two efficiencies. The peak values for the energy and exergy efficiencies are 81.5% and 76.2%, respectively. Based on the calculated limitation values, where the highest chemical energy (exergy) of the produced syngas and maximum achievable efficiencies are determined, a thermodynamically possible operating region is suggested.

Suggested Citation

  • Yueshi Wu & Weihong Yang & Wlodzimierz Blasiak, 2014. "Energy and Exergy Analysis of High Temperature Agent Gasification of Biomass," Energies, MDPI, vol. 7(4), pages 1-16, April.
    • Handle: RePEc:gam:jeners:v:7:y:2014:i:4:p:2107-2122:d:34613
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    References listed on IDEAS

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    8. Silva, Isabelly P. & Lima, Rafael M.A. & Silva, Gabriel F. & Ruzene, Denise S. & Silva, Daniel P., 2019. "Thermodynamic equilibrium model based on stoichiometric method for biomass gasification: A review of model modifications," Renewable and Sustainable Energy Reviews, Elsevier, vol. 114(C), pages 1-1.
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    12. Watson, Jamison & Zhang, Yuanhui & Si, Buchun & Chen, Wan-Ting & de Souza, Raquel, 2018. "Gasification of biowaste: A critical review and outlooks," Renewable and Sustainable Energy Reviews, Elsevier, vol. 83(C), pages 1-17.
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    14. Martínez González, Aldemar & Lesme Jaén, René & Silva Lora, Electo Eduardo, 2020. "Thermodynamic assessment of the integrated gasification-power plant operating in the sawmill industry: An energy and exergy analysis," Renewable Energy, Elsevier, vol. 147(P1), pages 1151-1163.
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    18. Goffé, Jonathan & Ferrasse, Jean-Henry, 2019. "Stoichiometry impact on the optimum efficiency of biomass conversion to biofuels," Energy, Elsevier, vol. 170(C), pages 438-458.
    19. Yang, Kun & Wang, Jiangjiang & Jiang, Haowen, 2024. "A novel exergy-based cost and carbon footprint allocation method in the multi-energy complementary system," Renewable Energy, Elsevier, vol. 231(C).

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