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A novel process for small-scale pipeline natural gas liquefaction

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  • He, T.B.
  • Ju, Y.L.

Abstract

A novel process for small-scale pipeline natural gas liquefaction is designed and presented. The novel process can utilize the pressure exergy of the pipeline to liquefy a part of natural gas without any energy consumption. The thermodynamic analysis including mass, energy balance and exergy analysis are adopted in this paper. The liquefaction rate and exergy utilization rate are chosen as the objective functions. Several key parameters are optimized to approach the maximum liquefaction rate and exergy utilization rate. The optimization results showed that the maximum liquefaction rate is 12.61% and the maximum exergy utilization rate is 0.1961. What is more, the economic performances of the process are also discussed and compared by using the maximum liquefaction rate and exergy utilization rate as indexes. In conclusion, the novel process is suitable for pressure exergy utilization due to its simplicity, zero energy consumption and short payback period.

Suggested Citation

  • He, T.B. & Ju, Y.L., 2014. "A novel process for small-scale pipeline natural gas liquefaction," Applied Energy, Elsevier, vol. 115(C), pages 17-24.
    • Handle: RePEc:eee:appene:v:115:y:2014:i:c:p:17-24
    DOI: 10.1016/j.apenergy.2013.11.016
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    References listed on IDEAS

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    2. Wang, Xucen & Li, Min & Cai, Liuxi & Li, Yun, 2020. "Propane and iso-butane pre-cooled mixed refrigerant liquefaction process for small-scale skid-mounted natural gas liquefaction," Applied Energy, Elsevier, vol. 275(C).
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    6. Uwitonze, Hosanna & Chaniago, Yus Donald & Lim, Hankwon, 2022. "Novel integrated energy-efficient dual-effect single mixed refrigerant and NGLs recovery process for small-scale natural gas processing plant," Energy, Elsevier, vol. 254(PA).
    7. Yao, Sheng & Zhang, Yufeng & Deng, Na & Yu, Xiaohui & Dong, Shengming, 2019. "Performance research on a power generation system using twin-screw expanders for energy recovery at natural gas pressure reduction stations under off-design conditions," Applied Energy, Elsevier, vol. 236(C), pages 1218-1230.
    8. Guo, Hao & Tang, Qixiong & Gong, Maoqiong & Cheng, Kuiwei, 2018. "Optimization of a novel liquefaction process based on Joule–Thomson cycle utilizing high-pressure natural gas exergy by genetic algorithm," Energy, Elsevier, vol. 151(C), pages 696-706.
    9. Yin, Liang & Ju, Yonglin, 2020. "Conceptual design and analysis of a novel process for BOG re-liquefaction combined with absorption refrigeration cycle," Energy, Elsevier, vol. 205(C).
    10. Yao, Sheng & Zhang, Yufeng & Yu, Xiaohui, 2018. "Thermo-economic analysis of a novel power generation system integrating a natural gas expansion plant with a geothermal ORC in Tianjin, China," Energy, Elsevier, vol. 164(C), pages 602-614.
    11. Zhang, Jinrui & Meerman, Hans & Benders, René & Faaij, André, 2020. "Technical and economic optimization of expander-based small-scale natural gas liquefaction processes with absorption precooling cycle," Energy, Elsevier, vol. 191(C).
    12. Ancona, M.A. & Bianchi, M. & Branchini, L. & De Pascale, A. & Melino, F. & Mormile, M. & Palella, M. & Scarponi, L.B., 2018. "Investigation on small-scale low pressure LNG production process," Applied Energy, Elsevier, vol. 227(C), pages 672-685.

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