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High Quality Syngas Production with Supercritical Biomass Gasification Integrated with a Water–Gas Shift Reactor

Author

Listed:
  • M. M. Sarafraz

    (School of Mechanical Engineering, University of Adelaide, Adelaide, Australia)

  • Mohammad Reza Safaei

    (Division of Computational Physics, Institute for Computational Science, Ton Duc Thang University, Ho Chi Minh City, Vietnam
    Faculty of Electrical and Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam)

  • M. Jafarian

    (School of Mechanical Engineering, University of Adelaide, Adelaide, Australia)

  • Marjan Goodarzi

    (Department of Mechanical Engineering, Lamar University, Beaumont, TX 77705, USA
    Sustainable Management of Natural Resources and Environment Research Group, Faculty of Environment and Labour Safety, Ton Duc Thang University, Ho Chi Minh City, Vietnam)

  • M. Arjomandi

    (School of Mechanical Engineering, University of Adelaide, Adelaide, Australia)

Abstract

A thermodynamic assessment is conducted for a new configuration of a supercritical water gasification plant with a water–gas shift reactor. The proposed configuration offers the potential for the production of syngas at different H 2 :CO ratios for various applications such as the Fischer–Tropsch process or fuel cells, and it is a path for addressing the common challenges associated with conventional gasification plants such as nitrogen dilution and ash separation. The proposed concept consists of two reactors, R 1 and R 2 , where the carbon containing fuel is gasified (in reactor R 1 ) and in reactor R 2 , the quality of the syngas (H 2 :CO ratio) is substantially improved. Reactor R 1 is a supercritical water gasifier and reactor R 2 is a water–gas shift reactor. The proposed concept was modelled using the Gibbs minimization method with HSC chemistry software. Our results show that the supercritical water to fuel ratio (SCW/C) is a key parameter for determining the quality of syngas (molar ratio of H 2 :CO) and the carbon conversion reaches 100%, when the SWC/C ratio ranges between two and 2.5 at 500–1000 °C.

Suggested Citation

  • M. M. Sarafraz & Mohammad Reza Safaei & M. Jafarian & Marjan Goodarzi & M. Arjomandi, 2019. "High Quality Syngas Production with Supercritical Biomass Gasification Integrated with a Water–Gas Shift Reactor," Energies, MDPI, vol. 12(13), pages 1-14, July.
    • Handle: RePEc:gam:jeners:v:12:y:2019:i:13:p:2591-:d:245854
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    References listed on IDEAS

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    Cited by:

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    2. Liu, Zhibin & Zhao, Chuankai & Cai, Longhao & Long, Xinman, 2022. "Steady state modelling of steam-gasification of biomass for H2-rich syngas production," Energy, Elsevier, vol. 238(PA).
    3. Jacek Grams, 2022. "Upgrading of Lignocellulosic Biomass to Hydrogen-Rich Gas," Energies, MDPI, vol. 16(1), pages 1-5, December.
    4. Liu, Shanke & Yang, Yan & Yu, Lijun & Cao, Yu & Liu, Xinyi & Yao, Anqi & Cao, Yaping, 2023. "Self-heating optimization of integrated system of supercritical water gasification of biomass for power generation using artificial neural network combined with process simulation," Energy, Elsevier, vol. 272(C).
    5. Odi Fawwaz Alrebei & Philip Bowen & Agustin Valera Medina, 2020. "Parametric Study of Various Thermodynamic Cycles for the Use of Unconventional Blends," Energies, MDPI, vol. 13(18), pages 1-16, September.
    6. Sanaye, Sepehr & Alizadeh, Pouria & Yazdani, Mohsen, 2022. "Thermo-economic analysis of syngas production from wet digested sewage sludge by gasification process," Renewable Energy, Elsevier, vol. 190(C), pages 524-539.
    7. Yao, Xiwen & Zhao, Zhicheng & Li, Jishuo & Zhang, Bohan & Zhou, Haodong & Xu, Kaili, 2020. "Experimental investigation of physicochemical and slagging characteristics of inorganic constituents in ash residues from gasification of different herbaceous biomass," Energy, Elsevier, vol. 198(C).
    8. Tang, Genyang & Gu, Jing & Huang, Zhen & Yuan, Haoran & Chen, Yong, 2022. "Cellulose gasification with Ca–Fe oxygen carrier in chemical-looping process," Energy, Elsevier, vol. 239(PD).

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