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- W131471763 abstract "In a previous work[1], moving boundary mass transfer inside a cylindrical capillary tube was properly modeled considering variable diffusion coefficient and no convective effects in the liquid phase. The numerical solution was semi-explicit because inside the finite difference matrix, the terms associated to the diffusion coefficients depend on the solute concentration. In the other hand, experimental results in that work showed such model it is not adequate to represent the mass transfer inside square capillaries, because convective flow patterns generated by square tube corners were not considered in the mass transfer model. In this work, the convective term was considered in the liquid phase and in the interface equations. The technique for solving the model was based in the methodology developed by Illingworth and Golosnoy [2] which allowed solute conservation and transformed the moving boundaries in fixed ones. Discretisation in liquid phase and interface equations was modified due the inclusion of the new term. Results showed that the experimental interface position inside the square glass capillary tube was well represented by this numerical model with convective effects. Simulation time (10 min) in this model is similar to the simulation time in the previous no convective model." @default.
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- W131471763 date "2007-03-22" @default.
- W131471763 modified "2023-09-23" @default.
- W131471763 title "Simple model for convective free boundary mass transfer inside a square capillary tube" @default.
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