Particulate fouling during the pool boiling heat transfer of MWCNT nanofluid

Xue, Huang; Fan, Jian Ren; Hu, Ya Cai; Hong, Rong Hua

doi:10.1007/s00231-011-0922-5

Cited by 2 publications

(1 citation statement)

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“…Recent developments in measurement and visualization techniques enable research at mini and micro scales as well as investigating complex flow structures. Recent scientific interest has focused particularly on two-phase flows in mini-and micro-channels [7][8][9][10][11] as well as on the boiling of nano-fluids to enhance heat transfer capability [12][13][14][15][16]. Experimental investigations have also been carried out on two-phase flows in the components of conventional heat exchange devices such as tubes, channels and walls.…”

Section: Introductionmentioning

confidence: 99%

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

2014

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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.

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