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An Experimental and Numerical Investigation of Fluidized Bed Gasification of Solid Waste

Author

Listed:
  • Sharmina Begum

    (School of Engineering and Technology, Central Queensland University, Rockhampton, QLD 4702, Australia)

  • Mohammad G. Rasul

    (School of Engineering and Technology, Central Queensland University, Rockhampton, QLD 4702, Australia)

  • Delwar Akbar

    (School of Business and Law, Central Queensland University, Rockhampton, QLD 4702, Australia)

  • David Cork

    (The Corky's Group, Mayfield, NSW 2304, Australia)

Abstract

Gasification is a thermo-chemical process to convert carbon-based products such as biomass and coal into a gas mixture known as synthetic gas or syngas. Various types of gasification methods exist, and fluidized bed gasification is one of them which is considered more efficient than others as fuel is fluidized in oxygen, steam or air. This paper presents an experimental and numerical investigation of fluidized bed gasification of solid waste (SW) (wood). The experimental measurement of syngas composition was done using a pilot scale gasifier. A numerical model was developed using Advanced System for Process ENgineering (Aspen) Plus software. Several Aspen Plus reactor blocks were used along with user defined FORTRAN and Excel code. The model was validated with experimental results. The study found very similar performance between simulation and experimental results, with a maximum variation of 3%. The validated model was used to study the effect of air-fuel and steam-fuel ratio on syngas composition. The model will be useful to predict the various operating parameters of a pilot scale SW gasification plant, such as temperature, pressure, air-fuel ratio and steam-fuel ratio. Therefore, the model can assist researchers, professionals and industries to identify optimized conditions for SW gasification.

Suggested Citation

  • Sharmina Begum & Mohammad G. Rasul & Delwar Akbar & David Cork, 2013. "An Experimental and Numerical Investigation of Fluidized Bed Gasification of Solid Waste," Energies, MDPI, vol. 7(1), pages 1-19, December.
  • Handle: RePEc:gam:jeners:v:7:y:2013:i:1:p:43-61:d:31636
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    References listed on IDEAS

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    1. Lee, Jong Min & Kim, Yong Jeon & Lee, Woon Jae & Kim, Sang Done, 1998. "Coal-gasification kinetics derived from pyrolysis in a fluidized-bed reactor," Energy, Elsevier, vol. 23(6), pages 475-488.
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    Cited by:

    1. Xianbin Xiao & Xueying Wang & Zongming Zheng & Wu Qin & Yumengqiu Zhou, 2019. "Catalytic Coal Gasification Process Simulation with Alkaline Organic Wastewater in a Fluidized Bed Reactor Using Aspen Plus," Energies, MDPI, vol. 12(7), pages 1-18, April.
    2. Jānis Krūmiņš & Māris Kļaviņš, 2023. "Integrated Circulating Fluidized Bed Gasification System for Sustainable Municipal Solid Waste Management: Energy Production and Heat Recovery," Energies, MDPI, vol. 16(13), pages 1-23, July.
    3. Ahmad, Anis Atikah & Zawawi, Norfadhila Abdullah & Kasim, Farizul Hafiz & Inayat, Abrar & Khasri, Azduwin, 2016. "Assessing the gasification performance of biomass: A review on biomass gasification process conditions, optimization and economic evaluation," Renewable and Sustainable Energy Reviews, Elsevier, vol. 53(C), pages 1333-1347.

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