Two-equation continuum model of drying appraised by comparison with pore network simulations

被引:2
作者
Ahmad, Faeez [1 ]
Prat, Marc [2 ]
Tsotsas, Evangelos [1 ]
Kharaghani, Abdolreza [1 ]
机构
[1] Otto von Guericke Univ, Univ Pl 2, D-39106 Magdeburg, Germany
[2] Univ Toulouse, Inst Mecan Fluides Toulouse IMFT, INPT, UPS,CNRS, F-31400 Toulouse, France
关键词
Two-equation continuum model; Pore network simulations; Scale transition; Non-local equilibrium effect; Porous media drying; POROUS-MEDIA; LOCAL EQUILIBRIUM; INTERFACIAL AREA; EVAPORATION; WATER; DIFFUSION; LIQUID; PERMEABILITY; EQUATIONS; HEAT;
D O I
10.1016/j.ijheatmasstransfer.2022.123073
中图分类号
O414.1 [热力学];
学科分类号
摘要
A two-equation non-local-equilibrium (NLE) continuum model of isothermal drying is assessed by comparison with pore network simulations considering a rigid capillary porous medium that is fully saturated initially. This continuum model consists of a transport equation for the liquid and of a transport equation for the vapor. The two main variables are the liquid saturation and the vapor partial pressure. The two equations are coupled by a phase-change term and mass transport at the medium surface is modeled by considering the individual boundary conditions for the two continuum model equations. The macroscopic parameters that appear in the NLE continuum model include classical parameters such as the effective liquid and vapor diffusivities, as well as non-classical and new parameters such as the specific interfacial area and the fraction of dry surface pores. These parameters are determined for the porous microstructure corresponding to the cubic network used to perform the pore network simulations. The results obtained by the two-equation NLE continuum model are compared with pore network simulation data. Comparisons reveal that the two-equation NLE continuum model can capture with a reasonable degree of accuracy the NLE effect as well as the phase distributions and drying kinetics of the pore network model drying simulations.
引用
收藏
页数:13
相关论文
共 52 条
[1]   Non-local equilibrium continuum modeling of partially saturated drying porous media: Comparison with pore network simulations [J].
Ahmad, Faeez ;
Talbi, Marouane ;
Prat, Marc ;
Tsotsas, Evangelos ;
Kharaghani, Abdolreza .
CHEMICAL ENGINEERING SCIENCE, 2020, 228
[2]  
[Anonymous], 2014, Handbook of Industrial Drying
[3]  
Bear J, 1991, INTRO MODELING TRANS
[4]  
Benet J.-C., 2009, J NON-EQUIL THERMODY, V34
[6]   Detailed physics, predictive capabilities and macroscopic consequences for pore-network models of multiphase flow [J].
Blunt, MJ ;
Jackson, MD ;
Piri, M ;
Valvatne, PH .
ADVANCES IN WATER RESOURCES, 2002, 25 (8-12) :1069-1089
[7]   Pore-scale characteristics of multiphase flow in porous media: A comparison of air-water and oil-water experiments [J].
Culligan, KA ;
Wildenschild, D ;
Christensen, BSB ;
Gray, WG ;
Rivers, ML .
ADVANCES IN WATER RESOURCES, 2006, 29 (02) :227-238
[8]   Measurement of interfacial area from NMR time dependent diffusion and relaxation measurements [J].
Fleury, M. .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2018, 509 :495-501
[9]  
Geoffroy S, 2014, BUILD PATHOL REHABIL, V4, P145, DOI 10.1007/978-3-319-04531-3_7
[10]  
Goeke A., 2013, RECENT TRENDS DYNAMI, V35