Abstract
Capillary pressure plays a critical role in driving fluid flow in unsaturated porous (pores not saturated with liquids but also containing air/gas) structures. The role and importance of capillary pressure have been well documented in geological and soil sciences but remain largely unexplored in the food literature. Available mathematical models for unsaturated food systems have either ignored the capillary-driven flow or combined it with the diffusive flow. Such approaches are bound to impact the accuracy of models. The derivation of the microscale definition of capillary pressure is overviewed, and the limitations of using the microscale definition at the macroscale are discussed. Next, the factors affecting capillary pressure are briefly reviewed. The parametric expressions for capillary pressure as a function of saturation and temperature, developed originally for soils, are listed, and their application for food systems is encouraged. Capillary pressure estimation methods used for food systems are then discussed. Next, the different mathematical formulations for food systems are compared, and the limitations of each formulation are discussed. Additionally, examples of hybrid mixture theory–based multiscale models for frying involving capillary pressure are provided. Capillary-driven liquid flow plays an important role in the unsaturated transport during the processing of porous solid foods. However, measuring capillary pressure in food systems is challenging because of the soft nature of foods. As a result, there is a lack of available capillary pressure data for food systems which has hampered the development of mechanistic models. Nevertheless, providing a fundamental understanding of capillary pressure will aid food engineers in designing new experimental studies and developing mechanistic models for unsaturated processes.
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Abbreviations
- \(A\) :
-
Pre-exponential factor (Eq. (43)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \(a\) :
-
Constant in the linear relation between \({\gamma }^{wn}\) and \(T\) (Eq. (22)) \((\mathrm{N}/\mathrm{m})\)
- \({a}_{s}\) :
-
Radius of sphere (Eq. (42)) (\(\mathrm{m}\))
- \({a}_{w}\) :
-
Water activity (Eq. (39)) (dimensionless)
- \({a}_{0}^{ws}\) :
-
Coefficient in the power series expression for the interfacial energy per unit area (Eq. (28)) \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \({a}_{0}^{ns}\) :
-
Coefficient in the power series expression for the interfacial energy per unit area (Eq. (29)) \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \({a}_{1}^{ws}\) :
-
Coefficient in the power series expression for the interfacial energy per unit area (Eq. (28)) \(\left(\frac{\mathrm{N}}{\mathrm{mK}}\right)\)
- \({a}_{1}^{ns}\) :
-
Coefficient in the power series expression for the interfacial energy per unit area (Eq. (29)) \(\left(\frac{\mathrm{N}}{\mathrm{mK}}\right)\)
- \(B\) :
-
Mixture viscosity of the biopolymeric matrix (Eq. (48)) (\(\mathrm{Pa}.\mathrm{s}\))
- \(b\) :
-
Constant in the linear relation between \({\gamma }^{wn}\) and \(T\) (Eq. (22)) \(\left(\frac{\mathrm{N}}{\mathrm{mK}}\right)\)
- \(C\) :
-
Liquid concentration (Eq. (40)) (amount of substance)
- \({C}_{0}\) :
-
Constant surface concentration (Eq. (42)) (amount of substance)
- \({C}_{1}\) :
-
Initial uniform concentration (Eq. (42)) (amount of substance)
- \({c}^{l}\) :
-
Mass concentration of liquid (Eq. (45)) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{3}}\right)\)
- \({c}^{ws}\) :
-
Constant (Eq. (30)) \(\left(\frac{\mathrm{N}}{\mathrm{mK}}\right)\)
- \({c}^{ns}\) :
-
Constant (Eq. (31)) \(\left(\frac{\mathrm{N}}{\mathrm{mK}}\right)\)
- \({C}_{p}^{\alpha }\) :
-
Specific heat for phase \(\alpha\) (Eq. (52)) \(\left(\frac{\mathrm{J}}{\mathrm{kgK}}\right)\)
- \({D}_{eff}\) :
-
Effective diffusivity (Eq. (43)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \({D}^{\alpha }\) :
-
Diffusivity of phase \(\alpha\) (Eq. (48)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \({D}_{c}\) :
-
Concentration gradient dependent capillary diffusivity (Eq. (46)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \({D}_{w}\) :
-
Capillary diffusivity of water (Eq. (47)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \({D}_{T}\) :
-
Temperature gradient dependent capillary diffusivity (Eq. (46)) \(\left(\frac{{\mathrm{m}}^{2}}{\mathrm{s}}\right)\)
- \({E}_{a}\) :
-
Activation energy (Eq. (43)) \(\left(\frac{\mathrm{J}}{\mathrm{mol}}\right)\)
- \(E\) :
-
Modulus of elasticity of the biopolymeric matrix (Eq. (48)) \((\mathrm{Pa})\)
- \({}^{\beta }{\widehat{e}}^{\alpha }\) :
-
Source-sink term (Eq. (49) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{3}\mathrm{s}}\right)\)
- \(F\) :
-
Resultant of the elastic surface forces acting on the contact line (Eq. (5)) \((\mathrm{N}/\mathrm{m})\)
- \(g\) :
-
Gravitational acceleration \((\mathrm{m}/{\mathrm{s}}^{2})\)
- \(h\) :
-
Capillary pressure head \((\mathrm{m})\)
- \({h}_{b}\) :
-
Bubbling pressure head (Eq. (1)\(9\)) \((\mathrm{m})\)
- \({\Delta }_{sn}^{sw}{h}^{s}\) :
-
Enthalpy of immersion per unit area (Eq. (21)) \((\mathrm{J}/{\mathrm{m}}^{2})\)
- \(I\) :
-
Identity tensor (Eq. (3)) (dimensionless)
- \({I}^{\sigma }\) :
-
\(I-NN\), Projected surficial identity tensor (Eq. (2)) (dimensionless)
- \({j}_{m}\) :
-
Mass flux of liquid phase (Eq. (44)) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{2}\mathrm{s}}\right)\)
- \({K}^{\alpha }\) :
-
Permeability of phase \(\alpha\) (Eq. (48)) \(({\mathrm{m}}^{2})\)
- \({k}^{\alpha }\) :
-
Thermal conductivity of phase \(\alpha\) (Eq. (52)) \(\left(\frac{\mathrm{W}}{\mathrm{mK}}\right)\)
- \(k\) :
-
Restriction on fitting parameters of van Genuchten’s function (Eq. (17)) (dimensionless)
- \(M\) :
-
Moisture content on a dry basis (Eq. (47)) \(\left(\frac{\mathrm{g}}{\mathrm{g solids}}\right)\)
- \({M}_{W}\) :
-
Molecular weight (Eq. (37)) \(\left(\frac{\mathrm{kg}}{\mathrm{mol}}\right)\)
- \(m\) :
-
Fitting parameter for van Genuchten’s function (Eq. (15)) (dimensionless)
- \(N\) :
-
Unit vector normal to the interface (towards \(\alpha\) phase) (Eq. (1)) (dimensionless)
- \(n\) :
-
Fitting parameter for van Genuchten’s function (Eq. (15)) (dimensionless)
- \({p}^{\alpha }\) :
-
Pressure of phase \(\alpha\) (Eq. (45)) \(\left(\frac{\mathrm{N}}{{\mathrm{m}}^{2}}\right)\)
- \({p}^{c}\) :
-
Microscale capillary pressure \((\mathrm{Pa})\)
- \({P}^{c}\) :
-
Macroscopic capillary pressure \((\mathrm{Pa})\)
- \(P\) :
-
Vapor pressure over the meniscus (Eq. (37)) \((\mathrm{Pa})\)
- \({P}_{0}\) :
-
Vapor pressure over the planar surface (Eq. (37)) \((\mathrm{Pa})\)
- \({P}^{b}\) :
-
Bubbling pressure (Eq. (18)) \((\mathrm{Pa})\)
- \(R\) :
-
Universal gas constant \(\left(\frac{\mathrm{J}}{\mathrm{mol K}}\right)\)
- \({R}_{c}\) :
-
Radius of curvature of the liquid surface in the tube (Eq. (37)) \((\mathrm{m})\)
- \(r\) :
-
Capillary radius \((\mathrm{m})\)
- \(r\) :
-
Radial distance \((\mathrm{m})\)
- \({S}_{w}\) :
-
Wetting phase saturation (dimensionless)
- \({S}_{e}\) :
-
Effective saturation of the wetting phase (dimensionless)
- \({S}_{s}\) :
-
Saturated wetting phase saturation (dimensionless)
- \({S}_{r}\) :
-
Residual wetting phase saturation (dimensionless)
- \({S}^{\alpha \beta }\) :
-
Interface stress tensor (Eq. (1)) \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \(s\) :
-
Distance (Eq. (44)) \(\left(\mathrm{m}\right)\)
- \({T}_{a}\) :
-
Stress tensor for adjacent phases (Eq. (1)) \(\left(\frac{\mathrm{N}}{{\mathrm{m}}^{2}}\right)\)
- \(T\) :
-
Temperature \((\mathrm{K})\)
- \({T}_{r}\) :
-
Reference temperature \((\mathrm{K})\)
- \({T}_{f}\) :
-
Target temperature \((\mathrm{K})\)
- \(U\) :
-
Velocity of the interface (Eq. (1)) \(\left(\frac{\mathrm{m}}{\mathrm{s}}\right)\)
- \({u}^{s,\alpha \beta }\) :
-
Interfacial energy per unit area for an interface formed by phase \(\alpha\) and \(\beta\) (Eq. (27)) \(\left(\frac{\mathrm{J}}{{\mathrm{m}}^{2}}\right)\)
- \({v}^{\alpha ,s}\) :
-
Velocity of \(\alpha\) phase with respect to the solid phase (Eq. (48)) \(\left(\frac{\mathrm{m}}{\mathrm{s}}\right)\)
- \({v}_{\alpha \beta }\) :
-
Normal to the contact line (Eq. (5)) (dimensionless)
- \({v}_{w}\) :
-
Molar volume of water (Eq. (39)) \(({\mathrm{m}}^{3}\mathrm{ mo}{\mathrm{l}}^{-1})\)
- \(v\) :
-
Velocity of adjacent phases at the interface (Eq. (1)) \(\left(\frac{\mathrm{m}}{\mathrm{s}}\right)\)
- \(\Gamma\) :
-
Excess mass of the interface (Eq. (1)) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{2}}\right)\)
- \(\rho\) :
-
Density \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{3}}\right)\)
- \({\rho }_{l}\) :
-
Liquid density (Eq. (37)) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{3}}\right)\)
- \({\rho }^{\alpha }\) :
-
Density of phase \(\alpha\) (Eq. (49)) \(\left(\frac{\mathrm{kg}}{{\mathrm{m}}^{3}}\right)\)
- \(\gamma\) :
-
Interfacial tension \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \({\gamma }^{wn}\) :
-
Interfacial tension between \(w\) and \(n\) (Eq. (2)) \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \(\Lambda\) :
-
Unit vector tangent to the contact line (Eq. (5)) (dimensionless)
- \({\tau }^{wn}\) :
-
Viscous stress tensor for \(wn\) interface (Eq. (2)) \(\left(\frac{\mathrm{N}}{\mathrm{m}}\right)\)
- \({\tau }^{\alpha }\) :
-
Viscous stress tensor for phase \(\alpha\) (Eq. (3)) \(\left(\frac{\mathrm{N}}{{\mathrm{m}}^{2}}\right)\)
- \({\gamma }^{wns}\) :
-
Contact curve compression (Eq. (5)) \(\left(\mathrm{N}\right)\)
- \(\theta\) :
-
Contact angle \((^\circ )\)
- \(\lambda\) :
-
Fitting parameter for Brooks and Corey’s expression (Eq. (18)) (dimensionless)
- \({\lambda }_{v}\) :
-
Latent heat of vaporization (Eq. (52)) \(\left(\frac{\mathrm{J}}{\mathrm{kg}}\right)\)
- \(\alpha\) :
-
Fitting parameter for van Genuchten’s function (Eq. (15)) \(\left(\frac{1}{\mathrm{m}}\right)\)
- \({\beta }_{0}\) :
-
Parameter in \({p}^{c}\left(T\right)\) expression (Eq. (33))
- \({\beta }_{1}\) :
-
Parameter in \({p}^{c}\left(T\right)\) expression (Eq. (33))
- \({\beta }_{2}\) :
-
Parameter in \({p}^{c}\left(T\right)\) expression (Eq. (33))
- \(\mu\) :
-
Dynamic viscosity \(\left(\mathrm{Pa}.\mathrm{s}\right)\)
- \({\mu }^{\alpha }\) :
-
Dynamic viscosity of phase \(\alpha\) (Eq. (48)) \(\left(\mathrm{Pa}.\mathrm{s}\right)\)
- \(\beta\) :
-
Angle formed by the capillary tube with the vertical direction (Eq. (35))
- \({\varepsilon }^{\alpha }\) :
-
Volume fraction of phase \(\alpha\) (Eq. (48)) (dimensionless)
- \(\dot{{\varepsilon }^{\alpha }}\) :
-
Material time derivative of volume fraction of phase \(\alpha\) with respect to the solid phase (Eq. (48)) \(\left({s}^{-1}\right)\)
- \(\phi\) :
-
Porosity (Eq. (51)) (dimensionless)
- \(\alpha\) :
-
General representation for a phase
- \(\beta\) :
-
General representation for a phase
- \(w\) :
-
Wetting phase
- \(n\) :
-
Non-wetting phase
- \(l\) :
-
Liquid
- \(w\) :
-
Water phase
- \(o\) :
-
Oil phase
- \(g\) :
-
Gas phase
- \(\frac{{D}^{\sigma }}{Dt}\) :
-
Surface material derivative (Eq. (1)) \((1/\mathrm{s})\)
- \({\nabla }^{\sigma }\) :
-
\({\nabla }^{\sigma }=\nabla -NN.\nabla\), Surface gradient operator (Eq. (1)) (\(1/\mathrm{m}\))
- \({\nabla }^{c}\) :
-
\({\nabla }^{\mathrm{c}}=\mathrm{\Lambda \Lambda }.\nabla\), Curvilineal del operator (Eq. (5)) (\(1/\mathrm{m}\))
- \(\langle \rangle\) :
-
Averaging operator (Eq. (12)) (dimensionless)
- \({D}^{s}/Dt\) :
-
Material time derivative with respect to the solid phase (Eq. (49)) (\(1/\mathrm{s}\))
- \(\left[\left[K\right]\right]\) :
-
\({\left[\left[K\right]\right]=K}^{\alpha }-{K}^{\beta }\), Jump in the quantity \(K\)
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The USDA-NIFA provided financial support under award numbers 20–67017-31194, ILLU-698–308, and ILLU-698–926.
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Y. S. wrote most of the manuscript text, reviewed the literature, gathered the figures, organized the contents, and acquired figure permissions. P. S. T. provided overall guidance, perceived the main idea, provided examples of applications to be incorporated, edited the text, and wrote parts of the manuscript.
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Shah, Y., Takhar, P.S. Capillary Pressure in Unsaturated Food Systems: Its Importance and Accounting for It in Mathematical Models. Food Eng Rev 15, 393–419 (2023). https://doi.org/10.1007/s12393-023-09341-7
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DOI: https://doi.org/10.1007/s12393-023-09341-7