Liquefied natural gas vaporizers serve as prominent regasification equipment in engineering receiving terminals. Nevertheless, the lack of comparative data and dimensionless correlations hinders the optimization of heat exchanger tubes for vaporizers. In this paper, the comprehensive regasification thermal-hydraulics performance of supercritical methane (S-CH4) in tubes with different structures—straight tube (ST), helical tube (HT) and coil tube (CT) is analyzed using computational fluid dynamics simulation methods. The variations of regasification thermodynamic parameters of S-CH4 in ST, HT and CT are revealed. The effects of the ratio of heat flux to mass flux, pressure, buoyancy and gravity on the regasification heat transfer of S-CH4 are also studied. Notably, the progressive supercritical boundary layer theory is adopted to explain performance differences. The key findings show that the curvature-induced centrifugal forces in HT and CT disrupt the symmetry of regasification kinetic parameters, enhancing the heat transfer coefficient by 28.5 % and 30.4 % compared to ST. As pressure increases, geometry-induced turbulence gradually diminishes relative to specific heat-driven thermal transport. ST exhibits the largest hydrodynamic boundary layer thickness with the upper part of 2.72 mm and the lower part of 1.74 mm due to buoyancy-driven stratification. ST demonstrates higher quantitative vorticity magnitudes in the boundary layer compared to HT and CT. Finally, three new dimensionless correlations incorporating a pseudo-boiling K number are respectively developed for S-CH4 in ST, HT and CT, yielding the expression of Nub = CRebn1Prbn2Kn3. The negative exponents (−0.0714, −0.0729 and −0.0549) for K number can effectively clarify enhanced regasification heat transfer of S-CH4 at elevated pressures. These findings can provide valuable insights for designing heat exchange tubes of vaporizers.
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