A novel 1D/2D model for simulating conjugate heat transfer applied to flow boiling in tubes with external fins

Abstract

This study presents a novel, simplified model for the time-efficient simulation of transient conjugate heat transfer in round tubes. The flow domain and the tube wall are modeled in 1D and 2D, respectively and empirical correlations are used to model the flow domain in 1D. The model is particularly useful when dealing with complex physics, such as flow boiling, which is the main focus of this study. The tube wall is assumed to have external fins. The flow is vertical upwards. Note that straightforward computational fluid dynamics (CFD) analysis of conjugate heat transfer in a system of tubes, leads to 3D modeling of fluid and solid domains. Because correlation is used and dimensionality reduced, the model is numerically more stable and computationally more time-efficient compared to the CFD approach. The benefit of the proposed approach is that it can be applied to large systems of tubes as encountered in many practical applications. The modeled equations are discretized in space using the finite volume method, with central differencing for the heat conduction equation in the solid domain, and upwind differencing of the convective term of the enthalpy transport equation in the flow domain. An explicit time discretization with forward differencing was applied to the enthalpy transport equation in the fluid domain. The conduction equation in the solid domain was time discretized using the CrankNicholson scheme. The model is applied in different boundary conditions and the predicted boiling patterns and temperature fields are discussed.

Numerical investigation of flow distribution in tubular space of fin-and-tube heat exchanger

“…The reason is the small volume of heat exchanger manifold. The flow maldistribution in heat exchanger tubes may result in high thermal stresses [11,12], as well as flow boiling [9,10] in a region where the flow rate is low. In literature, the flow maldistribution is heat exchangers is not studied extensively.…”

Numerical and experimental study of flow distribution in tubular space of fin-and-tube heat exchanger with modified inlet manifold

“…Therefore, it is needed to ensure the uniform flow distribution from the inlet manifold to heat exchanger tubes, to allow the correct operation of the device [13,14]. If the flow maldistribution occurs, then in case of large heat fluxes transferred, the flow boiling [9,10] may occur. The flow boiling in heat exchanger tubes may intensify the fouling (scaling) processes [8,11], which leads to excessive thermal stresses in tube bundle.…”

A numerical solution to an inverse unsteady-state heat transfer problem involving the Trefftz functions

“…A growing body of research is using advanced numerical analysis in simulations of heat and mass transport processes in channels. Experiments concerning time-dependent flow parameters are shown and discussed in, among others, [5][6][7][8][9].…”