4.7 Article

Analysis on the heat transfer performance of supercritical liquified natural gas in horizontal tubes during regasification process

Journal

ENERGY
Volume 262, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.energy.2022.125444

Keywords

Liquefied natural gas; Heat transfer; Diameter effect; Horizontal tube; Buoyancy effect

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This paper studied the heat transfer performance of liquefied natural gas (LNG) in the horizontal tube of a submerged combustion vaporizer (SCV). The effects of fluid temperature, mass flux, and tube diameter on heat transfer were comprehensively investigated through numerical simulation. The results showed that buoyancy significantly influenced the heat transfer performance, especially under low mass flux and large diameter conditions.
The submerged combustion vaporizer (SCV) is an indispensable peak-shaving heat exchanger in the regasification process of liquified natural gas (LNG). This paper mainly studies the trans-critical heat transfer performance of LNG in the horizontal tube of SCV under the convective heating condition. To this end, the conditions of fluid temperature, mass flux, and tube diameter are comprehensively investigated through numerical simulation. Based on the simulation results, the influence of the buoyancy on total and local heat transfer performance is analyzed from the distribution of flow field and thermal-physical property in the boundary layer. The results indicate that the buoyancy leads to a significant difference in convection thermal resistance around the circumference. Tube diameter and mass flux affect the degree of heat transfer strengthening in the lower part and heat transfer deterioration in the upper part of the tube, as well as the occupied circumferential proportion of the corresponding region. Considering the effects of local heat transfer strengthening and deterioration, buoyancy shows an enhancement effect overall on the heat transfer process, especially under the conditions of low mass flux and large diameter. Based on the mechanism analysis of the convective heat transfer, two correlations are proposed to calculate the local convection thermal resistance in the buoyancy strengthening and buoyancy deterioration region, respectively.

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