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A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 4: Sensitivity analysis of transport pressures and benchmarking with conventional technology for gas transport

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  • Aspelund, Audun
  • Gundersen, Truls

Abstract

A novel energy and cost effective transport chain for stranded natural gas utilized for power production with CO2 capture and storage is developed. It includes an offshore section, a combined gas carrier and an integrated receiving terminal. In the offshore section, natural gas (NG) is liquefied to LNG by liquid carbon dioxide (LCO2) and liquid inert nitrogen (LIN), which are used as cold carriers. In the onshore process, the cryogenic exergy in the LNG is utilized to cool and liquefy the cold carriers, LCO2 and LIN. The transport pressures for LNG, LIN and LCO2 will influence the thermodynamic efficiency as well as the ship utilization; hence sensitivity analyses are performed, showing that the ship utilization for the payload will vary between 58% and 80%, and the transport chain exergy efficiency between 48% and 52%. A thermodynamically optimized process requires 319Â kWh/tonne LNG. The NG lost due to power generation needed to operate the LEC processes is roughly one third of the requirement in a conventional transport chain for stranded NG gas with CO2 capture and sequestration (CCS).

Suggested Citation

  • Aspelund, Audun & Gundersen, Truls, 2009. "A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 4: Sensitivity analysis of transport pressures and benchmarking with conv," Applied Energy, Elsevier, vol. 86(6), pages 815-825, June.
    • Handle: RePEc:eee:appene:v:86:y:2009:i:6:p:815-825
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    References listed on IDEAS

    as
    1. Aspelund, Audun & Gundersen, Truls, 2009. "A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 2: The offshore and the onshore processes," Applied Energy, Elsevier, vol. 86(6), pages 793-804, June.
    2. Aspelund, Audun & Gundersen, Truls, 2009. "A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 1," Applied Energy, Elsevier, vol. 86(6), pages 781-792, June.
    3. Kvamsdal, Hanne M. & Jordal, Kristin & Bolland, Olav, 2007. "A quantitative comparison of gas turbine cycles with CO2 capture," Energy, Elsevier, vol. 32(1), pages 10-24.
    4. Li, H. & Yan, J., 2009. "Evaluating cubic equations of state for calculation of vapor-liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes," Applied Energy, Elsevier, vol. 86(6), pages 826-836, June.
    5. Li, H. & Yan, J. & Yan, J. & Anheden, M., 2009. "Impurity impacts on the purification process in oxy-fuel combustion based CO2 capture and storage system," Applied Energy, Elsevier, vol. 86(2), pages 202-213, February.
    6. Aspelund, Audun & Tveit, Steinar P. & Gundersen, Truls, 2009. "A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 3: The combined carrier and onshore storage," Applied Energy, Elsevier, vol. 86(6), pages 805-814, June.
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