Cited by 98Spacecraft and Cryogenic TechnologiesPhase Equilibria and ThermodynamicsHeat transfer and supercritical fluids

Simulation of boil-off losses during transfer at a LH2 based hydrogen refueling station

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Petitpas, Guillaume·2018·International Journal of Hydrogen Energy

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Crossref · 10.1016/j.ijhydene.2018.09.132

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1 of 1 references verified0 citation errors · 0 not checkable

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  • Petitpas's model ignores the insulation in the energy balance and assumes a constant rate of heat ingress into the tank.

    “This model ignores the insulation in the energy balance, instead assuming a constant rate of heat ingress into the tank; 50 W was found to yield the closest estimate to the experimental data.”

    From Modelling of Liquid Hydrogen Boil-Off (2022) · cites this paper as [27]

  • Tools that can accurately estimate BOG production are particularly important in the context of industrial-scale LH2 storage, as the capital expense to design and implement such systems is large, and experimental testing at a relevant pilot-scale can be cost-prohibitive with the results obtained making it difficult to translate to full-scale if their description is entirely empirical.

    “Tools that can accurately estimate BOG production are particularly important in the context of industrial-scale LH 2 storage, as the capital expense to design and implement such systems is large, and experimental testing at a relevant pilot-scale can be cost-prohibitive with the results obtained making it difficult to translate to full-scale if their description is entirely empirical [27,28].”

    From Modelling of Liquid Hydrogen Boil-Off (2022) · cites this paper as [27]

  • In the work of Petitpas, a 12.5 m3 LH2 Dewar tank with a 2 m internal diameter at the Lawrence Livermore Cryogenic Hydrogen Test Facility was subjected to ambient heat ingress to measure the change in liquid volume over summer versus winter.

    “In the work of Petitpas [27], a 12.5 m 3 LH 2 Dewar tank with a 2 m internal diameter at the Lawrence Livermore Cryogenic Hydrogen Test Facility was subjected to ambient heat ingress to measure the change in liquid volume over summer versus winter.”

    From Modelling of Liquid Hydrogen Boil-Off (2022) · cites this paper as [27]

  • U_VL = 0.15 W/m2/K was chosen for the model because it best matched the vapor temperature data reported by Petitpas.

    “A vapor-liquid heat transfer coefficient, U VL = 0.15 W/m 2 /K was chosen as this best matched the vapor temperature data reported by Petitpas [27].”

    From Modelling of Liquid Hydrogen Boil-Off (2022) · cites this paper as [27]

  • Throughout the Petitpas experiment, the system remained static, meaning no mass transfer across the system boundary occurred.

    “Throughout the experiment, the system remained 'static', meaning no mass transfer across the system boundary (such as refuelling) occurred.”

    From Modelling of Liquid Hydrogen Boil-Off (2022) · cites this paper as [27]

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Authors
Petitpas, G.
Affiliations
Lawrence Livermore National Laboratory (US)
Corresponding author
Petitpas, Guillaume
Venue
International Journal of Hydrogen Energy
Publisher
Elsevier BV
Published
2018-11
Volume
43
Issue
46
Pages
21451-21463
ISSN
0360-3199 (ISSN-L)
OpenAlex
W2897362906
Cited by
98
References
1
Citations by year
2026: 22 · 2025: 20 · 2024: 19 · 2023: 13 · 2022: 13 · 2021: 4 · 2020: 4 · 2019: 3
FWCI
2.24
Type
journal article
Language
en
Open access
Locations
  • International Journal of Hydrogen Energy (acceptedVersion)
  • OSTI OAI (U.S. Department of Energy Office of Scientific and Technical Information) (submittedVersion)
Funders
  • US Department of Energy
  • Fuel Cell Technologies Office
Topics
  • Physical Sciences › Engineering › Aerospace Engineering › Spacecraft and Cryogenic Technologies
  • Physical Sciences › Engineering › Biomedical Engineering › Phase Equilibria and Thermodynamics
  • Physical Sciences › Engineering › Computational Mechanics › Heat transfer and supercritical fluids
Keywords
liquid hydrogen, hydrogen refueling stations, two-phase flow, evaporation and condensation, real gas equation of state, REFPROP, subcooled liquid, vapor compression, hydrogen venting, heat transfer

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