Modelling Liquid Hydrogen Boil-Off Rate

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SUMMARY

The forum discussion focuses on modeling the boil-off rate of liquid hydrogen using the boilFAST simulation tool. Users report encountering unrealistic negative spikes in boil-off rates, indicating an increase in liquid volume, which is physically impossible. Key parameters include a horizontal cylinder tank with hemispherical end caps, a volume of 30.02 m³, and an initial liquid volume of 29.44 m³. The thermal conductivity of the insulation is 0.00009 W m-2 K-1, with a heat transfer coefficient of 0.0021 W m-2 K-1, leading to a calculated heating rate of approximately 28.5 W.

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  • Understanding of thermal conductivity and heat transfer coefficients
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  • Knowledge of cylindrical tank geometry and insulation effects
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JB312
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TL;DR
I am working on modelling the liquid hydrogen boil-off for a storage tank (30m3) over a period of 2.5 hours using three different insulation materials - polyurethane foam, aerogel, and MLI.
The relevant thermal conductivity, heat transfer coefficients, and thicknesses along with all other required parameters are known. I have attempted to use the online simulation tool boilFAST to simulate each scenario however, the results show a negative spike in boil-off rate which I don't see being possible as this would imply that there is an increase in the volume of liquid hydrogen. Does anyone have any experience in modelling similar scenarios or know another simulation tool that might be useful? Thanks in advance.
 
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Please provide the data on heat transfer coefficients, thicknesses, thermal conductivities, shape. Also, starting mass- or volume fraction of liquid and starting temperature or pressure.
 
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Certainly. Shape = horizontal cylinder with hemispherical end caps, volume = 30.02 m^3, initial liquid volume = 29.44 m^3, inner diameter = 2.93 m, length = 2.5 m (cylinder), relief pressure = 0.25 MPa, liquid temp = 20 K, pressure = 0.092 MPa, ambient temp = 293.15 K, insulation (MLI) thermal conductivity k = 0.00009 W m^-2 K^-1, thickness = 42.7 mm, corresponding heat transfer coefficient (k/thickness) = 0.0021 W m^-2 K^-1. Thank you very much for any help.
 
What is the tank made of, and what is its wall thickness?
 
Thermodynamic data on H2 are given in this reference: https://nvlpubs.nist.gov/nistpubs/Legacy/MONO/nbsmonograph168.pdf
The surface area for heat transfer is about 50 M^2, so the rate of heating is on the order of $$\dot{Q}=50(0.0021)(293-22)=28.5 W=102\ kJ/hr$$
The specific volume of liquid H2 at 20 K is 0.01412 m^3/kg, so the mass of liquid H2 originally in the tank is 29.44/0.01412 = 2085 kg.. At these temperatures, the heat of vaporization is about 450 kJ/kg, So, in 2.5 hours, roughly 0.6 kg would boil off.
 
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