CFD Simulation of Pressure Reduction Inside Large-scale Liquefied Hydrogen Tank
Abstract
Building the international hydrogen supply chain requires the large-scale liquefied hydrogen(LH2) carrier. During shipping LH2 with LH2 Carrier, the tank is pressurized by LH2 evaporation due to heat ingress from outside. Before unloading LH2 at the receiving terminal, reducing the tank pressure is essential for the safe tank operation. However, pressure reduction might cause flashing, leading to rapid vaporization of liquefied hydrogen, liquid leakage. Moreover, it was considered that pressure recovery phenomenon which was not preferred in terms of tank pressure management occurred at the beginning of pressure reduction. Hence, the purpose of our research is to clarify the phenomenon inside the cargo tank during pressure reduction. The CFD analysis of the pressure reduction phenomenon was conducted with the VOF based in-house CFD code, utilizing the C-CUP scheme combined with the hybrid Level Set and MARS method. In our previous research, the pressure reduction experiments with the 30 m³ LH2 tank were simulated, and the results showed that the pressure recovery was caused by the boiling delay, and the tank pressure followed the saturation pressure after the liquid was fully stirred. In this paper, the results were re-evaluated in terms of temperature. While pressure reduction was dominant, the temperature of vapor-liquid interface decreased. Once the boiling bubble stirred the interface, its temperature reached the saturation temperature after pressure recovery occurred. Moreover, it was found that the liquid temperature during pressure reduction could not be measured because of the boiling from the wall of the thermometer. The CFD analysis on pressure reduction of 1250 m³ tank for the LH2 Carrier was also very could occur in the case of the 1250 m³ tank in a certain condition. These results provide new insight into the development of the LH2 carrier.