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Advanced exergy analysis of novel flash based Helium recovery from natural gas processes

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  • Mehrpooya, Mehdi
  • Shafaei, Arash

Abstract

Two cryogenic Helium recovery processes which are based on the flash separation are investigated and analyzed. The presence of Helium in the natural gas affects shape of its phase envelope. Effect of various components concentration on the natural gas phase envelope shape is investigated. Two modified cryogenic flash based processes are introduced. Two new parameters are proposed in order to evaluate performance of the under consideration processes. Modified processes are investigated by the exergy analysis method. Exergy loss and exergy efficiency of the process components are calculated. Results show that the compressors have the lowest exergy loss in both processes. In the compressors high portion of exergy destruction is related to the avoidable part that means this exergy destruction can be decreased. But in the multi stream heat exchangers high portion of exergy destruction is related to the unavoidable exergy destruction. Endogenous/exogenous destructions shows that portion of endogenous exergy destruction in the components is higher than the exogenous part. In fact interactions among the components do not affect the inefficiencies significantly.

Suggested Citation

  • Mehrpooya, Mehdi & Shafaei, Arash, 2016. "Advanced exergy analysis of novel flash based Helium recovery from natural gas processes," Energy, Elsevier, vol. 114(C), pages 64-83.
    • Handle: RePEc:eee:energy:v:114:y:2016:i:c:p:64-83
    DOI: 10.1016/j.energy.2016.07.169
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    References listed on IDEAS

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    1. Querol, E. & Gonzalez-Regueral, B. & Ramos, A. & Perez-Benedito, J.L., 2011. "Novel application for exergy and thermoeconomic analysis of processes simulated with Aspen Plus®," Energy, Elsevier, vol. 36(2), pages 964-974.
    2. Tesch, Stefanie & Morosuk, Tatiana & Tsatsaronis, George, 2016. "Advanced exergy analysis applied to the process of regasification of LNG (liquefied natural gas) integrated into an air separation process," Energy, Elsevier, vol. 117(P2), pages 550-561.
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    4. Mehrpooya, Mehdi & Moftakhari Sharifzadeh, Mohammad Mehdi & Rosen, Marc A., 2015. "Optimum design and exergy analysis of a novel cryogenic air separation process with LNG (liquefied natural gas) cold energy utilization," Energy, Elsevier, vol. 90(P2), pages 2047-2069.
    5. Mehrpooya, Mehdi & Moftakhari Sharifzadeh, Mohammad Mehdi & Rosen, Marc A., 2016. "Energy and exergy analyses of a novel power cycle using the cold of LNG (liquefied natural gas) and low-temperature solar energy," Energy, Elsevier, vol. 95(C), pages 324-345.
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    Cited by:

    1. Ghorbani, Bahram & Shirmohammadi, Reza & Mehrpooya, Mehdi & Mafi, Mostafa, 2018. "Applying an integrated trigeneration incorporating hybrid energy systems for natural gas liquefaction," Energy, Elsevier, vol. 149(C), pages 848-864.
    2. Shafaei, Arash & Mehrpooya, Mehdi, 2018. "Process development and sensitivity analysis of novel integrated helium recovery from natural gas processes," Energy, Elsevier, vol. 154(C), pages 52-67.
    3. Mehrpooya, Mehdi & Shahsavan, Mohsen & Sharifzadeh, Mohammad Mehdi Moftakhari, 2016. "Modeling, energy and exergy analysis of solar chimney power plant-Tehran climate data case study," Energy, Elsevier, vol. 115(P1), pages 257-273.
    4. Zonouz, Masood Jalali & Mehrpooya, Mehdi, 2017. "Parametric study of a hybrid one column air separation unit (ASU) and CO2 power cycle based on advanced exergy cost analysis results," Energy, Elsevier, vol. 140(P1), pages 261-275.
    5. Erbay, Zafer & Hepbasli, Arif, 2017. "Assessment of cost sources and improvement potentials of a ground-source heat pump food drying system through advanced exergoeconomic analysis method," Energy, Elsevier, vol. 127(C), pages 502-515.
    6. Fallah, M. & Siyahi, H. & Ghiasi, R. Akbarpour & Mahmoudi, S.M.S. & Yari, M. & Rosen, M.A., 2016. "Comparison of different gas turbine cycles and advanced exergy analysis of the most effective," Energy, Elsevier, vol. 116(P1), pages 701-715.

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