TY - JOUR
T1 - Liquid hydrogen storage and regasification process integrated with LNG, NGL, and liquid helium production
AU - Naquash, Ahmad
AU - Riaz, Amjad
AU - Qyyum, Muhammad Abdul
AU - Aziz, Muhammad
AU - Assareh, Ehsanolah
AU - Lee, Moonyong
N1 - Publisher Copyright:
© 2023 Elsevier Ltd
PY - 2023/9/1
Y1 - 2023/9/1
N2 - Hydrogen (H2) is a clean energy carrier and has recently gained significant attention. Efforts are being made to promote liquid hydrogen (LH2) owing to its long-time storage, transportation, and high-purity end-use requirements. LH2 storage and regasification is an essential step in the H2 supply chain. This study proposes a novel integrated energy system that produces liquefied natural gas (LNG), natural gas liquids (NGL), and liquid helium (LHe) utilizing the cold energy of LH2. A well-known process simulation software (Aspen Hysys® v11) is employed to simulate the integrated process. The optimal design variables are found through the Aspen Hysys® built-in Mixed optimization technique. The optimal design shows a specific energy consumption of 0.347 kWh/kg with exergy destruction of 43.3 MW. The required volume of the spherical tank for LH2 storage is 6.3 m3. The results of the lifecycle cost analysis show that the Levelized cost of producing LNG, NGL, and LHe is 0.50 USD/kg, 0.56 USD/kg, and 98.0 USD/kg, respectively. The conclusion of this study suggests that the proposed process can improve the overall H2 supply chain by effectively utilizing LH2 for LNG, NGL, and LHe production.
AB - Hydrogen (H2) is a clean energy carrier and has recently gained significant attention. Efforts are being made to promote liquid hydrogen (LH2) owing to its long-time storage, transportation, and high-purity end-use requirements. LH2 storage and regasification is an essential step in the H2 supply chain. This study proposes a novel integrated energy system that produces liquefied natural gas (LNG), natural gas liquids (NGL), and liquid helium (LHe) utilizing the cold energy of LH2. A well-known process simulation software (Aspen Hysys® v11) is employed to simulate the integrated process. The optimal design variables are found through the Aspen Hysys® built-in Mixed optimization technique. The optimal design shows a specific energy consumption of 0.347 kWh/kg with exergy destruction of 43.3 MW. The required volume of the spherical tank for LH2 storage is 6.3 m3. The results of the lifecycle cost analysis show that the Levelized cost of producing LNG, NGL, and LHe is 0.50 USD/kg, 0.56 USD/kg, and 98.0 USD/kg, respectively. The conclusion of this study suggests that the proposed process can improve the overall H2 supply chain by effectively utilizing LH2 for LNG, NGL, and LHe production.
KW - Helium liquefaction
KW - Liquid hydrogen regasification
KW - Liquid hydrogen storage
KW - Natural gas liquefaction
KW - Natural gas liquids
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UR - https://www.mendeley.com/catalogue/a81d8f95-6186-3c2d-82c2-a32df787a532/
U2 - 10.1016/j.renene.2023.05.122
DO - 10.1016/j.renene.2023.05.122
M3 - Article
AN - SCOPUS:85161638249
SN - 0960-1481
VL - 213
SP - 165
EP - 175
JO - Renewable Energy
JF - Renewable Energy
ER -