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Controlling Parameters in the Efficiency of Hydrogen Production via Electrification with Multi-Phase Plasma Processing Technology

Author

Listed:
  • Shariful Islam Bhuiyan

    (Department of Mechanical Engineering, Texas A&M University, College Station, TX 77843, USA)

  • Kunpeng Wang

    (LTEOIL, LLC, 2929 Allen Parkway, Suite 200, Houston, TX 77019, USA)

  • Md Abdullah Hil Baky

    (Department of Mechanical Engineering, Texas A&M University, College Station, TX 77843, USA)

  • Jamie Kraus

    (Department of Mechanical Engineering, Texas A&M University, College Station, TX 77843, USA)

  • Howard Jemison

    (LTEOIL, LLC, 2929 Allen Parkway, Suite 200, Houston, TX 77019, USA)

  • David Staack

    (Department of Mechanical Engineering, Texas A&M University, College Station, TX 77843, USA)

Abstract

A nanosecond pulsed non-equilibrium plasma reactor is used to crack hydrocarbons into hydrogen and lighter intermediates at atmospheric pressure and warm temperature. The effects of power, capacitance, breakdown voltage, pulsing frequency, energy per pulse, and carrier gas type are investigated for product generation. Multiple gaseous products including hydrogen and hydrocarbons are calculated and compared at different conditions. A statistical analysis is performed on hydrogen yield for different experimental conditions to determine the significance of the studied parameters. Comparable hydrogen yields are produced when using methane (4 to 22 g-H 2 /kWh) as a carrier gas as compared to argon (7 to 14 g-H 2 /kWh). Although, notably, the methane carrier is more selective to hydrogen and sensitive to other operating parameters, the argon is not. Statistical analysis shows that plasma power, capacitance, and energy per pulse appear to influence hydrogen yield while pulsing frequency and breakdown voltage do not. A higher yield of hydrogen is achieved with low plasma power and a low energy per pulse, with a low capacitance for both cases of pure CH 4 and pure Ar. The results show that low plasma power based on a low energy per pulse of <10 mJ is preferable for hydrogen production in a batch reactor. This CO 2 -free hydrogen production method produces hydrogen from fossil fuels at less than USD 2/kg in electricity.

Suggested Citation

  • Shariful Islam Bhuiyan & Kunpeng Wang & Md Abdullah Hil Baky & Jamie Kraus & Howard Jemison & David Staack, 2023. "Controlling Parameters in the Efficiency of Hydrogen Production via Electrification with Multi-Phase Plasma Processing Technology," Energies, MDPI, vol. 16(14), pages 1-15, July.
    • Handle: RePEc:gam:jeners:v:16:y:2023:i:14:p:5509-:d:1198583
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    References listed on IDEAS

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    2. Quarton, Christopher J. & Samsatli, Sheila, 2020. "The value of hydrogen and carbon capture, storage and utilisation in decarbonising energy: Insights from integrated value chain optimisation," Applied Energy, Elsevier, vol. 257(C).
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    4. Wang, Qiuying & Zhu, Xiaomei & Sun, Bing & Li, Zhi & Liu, Jinglin, 2022. "Hydrogen production from methane via liquid phase microwave plasma: A deoxidation strategy," Applied Energy, Elsevier, vol. 328(C).
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    Cited by:

    1. Xiangnan Cao & Guiying Song & Yikai Chen & Haowei Chen, 2024. "Research on Solid-State Linear Transformer Driver Power Source Driving Atmospheric Pressure Plasma Jet Treatment of Epoxy Resin," Energies, MDPI, vol. 17(18), pages 1-12, September.
    2. Henryka Danuta Stryczewska & Grzegorz Komarzyniec & Oleksandr Boiko, 2024. "Effect of Plasma Gas Type on the Operation Characteristics of a Three-Phase Plasma Reactor with Gliding Arc Discharge," Energies, MDPI, vol. 17(11), pages 1-19, June.

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