Abstract
Presents a two-dimensional unsteady model of heat transfer in terms of condensation of natural gas at low temperatures. Performed calculations of the process heat and mass transfer of liquefied natural gas (LNG) storage tanks of cylindrical shape. The influence of model parameters on the nature of heat transfer. Defined temperature regimes eliminate evaporation by liquefied natural gas. The obtained dependence of the mass flow rate of vapor condensation gas temperature. Identified the possibility of regulating the process of cooling down liquefied natural gas in terms of its partial evaporation with low cost energy.
Highlights
Presents a two-dimensional unsteady model of heat transfer in terms of condensation of natural gas at low temperatures
The occurrence of high temperature gradients in this area complicates the numerical analysis of the process of heat transfer under conditions of intensive phase transformations
The purpose of this work is the solution of heat and mass transfer under the conditions of condensation of natural gas at low temperatures
Summary
Presents a two-dimensional unsteady model of heat transfer in terms of condensation of natural gas at low temperatures. Performed calculations of the process heat and mass transfer of liquefied natural gas (LNG) storage tanks of cylindrical shape.
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