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Combined fluidized bed retorting and circulating fluidized bed combustion system of oil shale: 2. Energy and economic analysis

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  • Han, Xiangxin
  • Niu, Mengting
  • Jiang, Xiumin

Abstract

Retorting oil shale can produce shale oil, semicoke, water and fuel gases. Shale oil can be used as an important substitute oil supply, and semicoke and fuel gases may be burnt as fuels. An interesting issue is about how to utilize and distribute the heat from the combustion of semicoke and fuel gases, not only providing enough heat for retorting oil shale, but also producing more available energy products and less energy losses. Based on a combined system of oil shale FB (fluidized bed) retort and semicoke CFB (circulating fluidized bed) boiler, a comprehensive process flow was developed and an optimization calculation was conducted to achieve mass and energy balances of the whole system. Simulation indicated that, burning semicoke and fuel gases from retorting Huadian oil shale at the retorting temperature of 490 °C could not only provide enough energy required for the endothermic oil shale drying and retorting processes, but also supply extra energy for power generation or heat supply. The sensitivity of various operating parameters on the performance of the process was also discussed to optimize the comprehensive utilization system of oil shale. This work provided a reference for developing the new comprehensive utilization technology of oil shale.

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  • Han, Xiangxin & Niu, Mengting & Jiang, Xiumin, 2014. "Combined fluidized bed retorting and circulating fluidized bed combustion system of oil shale: 2. Energy and economic analysis," Energy, Elsevier, vol. 74(C), pages 788-794.
  • Handle: RePEc:eee:energy:v:74:y:2014:i:c:p:788-794
    DOI: 10.1016/j.energy.2014.07.050
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    References listed on IDEAS

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    Cited by:

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    2. Yang, Qingchun & Qian, Yu & Kraslawski, Andrzej & Zhou, Huairong & Yang, Siyu, 2016. "Framework for advanced exergoeconomic performance analysis and optimization of an oil shale retorting process," Energy, Elsevier, vol. 109(C), pages 62-76.
    3. Niu, Daming & Sun, Pingchang & Ma, Lin & Zhao, Kang'an & Ding, Cong, 2023. "Porosity evolution of Minhe oil shale under an open rapid heating system and the carbon storage potentials," Renewable Energy, Elsevier, vol. 205(C), pages 783-799.
    4. Yang, Qingchun & Qian, Yu & Kraslawski, Andrzej & Zhou, Huairong & Yang, Siyu, 2016. "Advanced exergy analysis of an oil shale retorting process," Applied Energy, Elsevier, vol. 165(C), pages 405-415.
    5. Wei Guo & Zhendong Wang & Youhong Sun & Xiaoshu Lü & Yuan Wang & Sunhua Deng & Qiang Li, 2020. "Effects of Packer Locations on Downhole Electric Heater Performance: Experimental Test and Economic Analysis," Energies, MDPI, vol. 13(2), pages 1-17, January.
    6. Jiang, Yongdong & Luo, Yahuang & Lu, Yiyu & Qin, Chao & Liu, Hui, 2016. "Effects of supercritical CO2 treatment time, pressure, and temperature on microstructure of shale," Energy, Elsevier, vol. 97(C), pages 173-181.
    7. Sun, Youhong & Bai, Fengtian & Lü, Xiaoshu & Jia, Chunxia & Wang, Qing & Guo, Mingyi & Li, Qiang & Guo, Wei, 2015. "Kinetic study of Huadian oil shale combustion using a multi-stage parallel reaction model," Energy, Elsevier, vol. 82(C), pages 705-713.
    8. Peng, Wanxi & Liu, Zhenling & Motahari-Nezhad, Mohsen & Banisaeed, Mohammad & Shahraki, Saeid & Beheshti, Mehdi, 2016. "A detailed study of oxy-fuel combustion of biomass in a circulating fluidized bed (CFB) combustor: Evaluation of catalytic performance of metal nanoparticles (Al, Ni) for combustion efficiency improve," Energy, Elsevier, vol. 109(C), pages 1139-1147.
    9. Li, Xiuxi & Zhou, Huairong & Wang, Yajun & Qian, Yu & Yang, Siyu, 2015. "Thermoeconomic analysis of oil shale retorting processes with gas or solid heat carrier," Energy, Elsevier, vol. 87(C), pages 605-614.
    10. Mu, Mao & Han, Xiangxin & Jiang, Xiumin, 2018. "Combined fluidized bed retorting and circulating fluidized bed combustion system of oil shale: 3. Exergy analysis," Energy, Elsevier, vol. 151(C), pages 930-939.

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