Influence of pore-network microstructure on the isothermal-drying performance of porous media

2021 ◽  
pp. 1-14
Author(s):  
Zhenyu Xu ◽  
Krishna M. Pillai
2014 ◽  
Vol 2014 ◽  
pp. 1-8 ◽  
Author(s):  
Yuan Yuejin ◽  
Zhao Zhe ◽  
Nie Junnan ◽  
Xu Yingying

In view of the fact that the zone model for porous media drying cannot disclose the mechanism of liquid phase distribution effectively, a pore network model for the slow isothermal drying process of porous media was developed by applying the theories of pore network drying and transport-process, which fused the physical parameters of porous media, such as porosity, pore mean diameter, and pore size distribution into the model parameters, and a sand bed drying experiment was conducted to verify the validity of this model. The experiment and simulation results indicate that the pore network model could explain the slow isothermal drying process of porous media well. The pore size distributions of porous media have a great effect on the liquid phase distribution of the drying process. The dual-zone model is suitable for the porous media whose pore size distribution obeys Gaussian distribution, while the three-zone model is suitable for the porous media whose pore size distribution obeys the lognormal distribution when the drying analysis of porous media is conducted.


2012 ◽  
Vol 538-541 ◽  
pp. 538-541 ◽  
Author(s):  
Ying Ying Xu ◽  
Yue Ding Yuan ◽  
Yue Jin Yuan ◽  
Xin An Dang ◽  
Xiang Dong Liu

Taking the sand bed as the simulated object, a pore network model for drying of real porous media is developed by applying the invasion percolation theory and transport process principle, which fused the physical parameters of sand bed, such as porosity, pore mean diameter, pore size distribution, into the model parameters. The experiment and simulation results indicated that this model could explain the drying process of sand bed well. The throat size distribution has a great effect on the drying process.


Author(s):  
A. G. Yiotis ◽  
A. K. Stubos ◽  
A. G. Boudouvis ◽  
N. Tsimpanogiannis ◽  
Y. C. Yortsos

2001 ◽  
Author(s):  
A. G. Yiotis ◽  
A. K. Stubos ◽  
A. G. Boudouvis ◽  
Y. C. Yortsos

Abstract A pore network model for the drying of capillary porous media is presented in this work. The model accounts for various processes at the pore scale including evaporation of a volatile liquid, mass transfer of the vapors by advection and diffusion in the gas phase and viscous flow in the liquid and gas phases. Both viscous and capillary forces at the liquid menisci in pore throats are also modeled. We consider isothermal drying in a rectilinear horizontal geometry, with no flow conditions in all but one boundary, at which a purge gas is injected at a constant rate. Drying rates, phase distribution and concentration patterns are reported as a function of time and the gas flow rate. We also refer to the evolution of trapped liquid clusters.


Author(s):  
Vikranth Kumar Surasani ◽  
Githin Tom Zachariah ◽  
Debashis Panda

Modeling of dring of capillary porous media is difficult due to the complex and coupled heat and mass transfer that occur at dynamic liquid-gas-sold interface. Thus far, drying was simulated using either continuum models or pore-network models, both of which have limitations. In this work, the Lattice Boltzmann Method (LBM) is used to simulate the drying in porous media. The LBM is ideal for such simulations as it can incorporate complex effects in a simple way to exhibit realistic fluid-gas interface during drying of capillary porous media. Keywords: Lattice Boltzmann Method; Capillary Porous media; Drying, Pore Network.  


2005 ◽  
Vol 58 (1-2) ◽  
pp. 63-86 ◽  
Author(s):  
A. G. Yiotis ◽  
A. K. Stubos ◽  
A. G. Boudouvis ◽  
I. N. Tsimpanogiannis ◽  
Y. C. Yortsos

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