Abstract
We present a systematic, quantitative assessment of the impact of pore size disorder and its interplay with flow rates and wettability on immiscible displacement of a viscous fluid. Porescale simulations and micromodel experiments show that reducing disorder increases the displacement efficiency and compactness, minimizing the fluidfluid interfacial area, through (i) trapping at low rates and (ii) viscous fingering at high rates. Increasing the wetting angle suppresses both trapping and fingering, hence reducing the sensitivity of the displacement to the underlying disorder. A modified capillary number Ca^{*} that includes the impact of disorder λ on viscous forces (through pore connectivity) is direct related to λ, in par with previous works. Our findings bear important consequences on sweep efficiency and fluid mixing and reactions, which are key in applications such as microfluidics to carbon geosequestration, energy recovery, and soil aeration and remediation.
Similar content being viewed by others
Introduction
In many of the challenges we face today as geoscientists, in particular in the context of water and energy resources, fluid invasion into a porous soil or sediment is a key process. Examples include hydrocarbon migration and recovery, methane venting from hydratebearing sediments, drying and wetting of soils, and carbon geosequestration^{1}. Fluid displacement has also gained attention as a scientific paradigm for problems where competitive domain growth and nonlinear interface dynamics are influenced by spatial heterogeneity of the system properties, such as magnetic domains and biological films^{2}.
The complex interplay between capillary, viscous, and gravitational forces, wettability effects, and the underlying heterogenous pore geometry, leads to ramified, preferential flow paths or “fingering”. Predicting the emergent patterns is challenging, because of the sensitivity to porescale details and the large number of coupled mechanisms and governing parameters which vary over a wide range of values and scales^{3,4}. Fingering leaves pockets of the original, defending fluid, increasing the fluidfluid interfacial area, with important consequences on efficiency of processes relying on fluid withdrawal such as enhanced hydrocarbon recovery^{5}, or on fluid mixing and reaction such as subsurface remediation^{6} or CO_{2} sequestration^{7}.
The practical importance of fluid displacement motivated intensive research, that identified several important mechanisms governing the displacement efficiency. In disordered media, slow displacement of a wetting fluid (by a less wetting fluid, termed “drainage”) leads to a patchy pattern with multiple islands of defending fluid, called capillary fingering (CF). The process of forming these islands is called trapping, as lack of fluid continuity between them inhibits their mobilization. Increasing the flow rate (hence the strength of viscous forces relative to capillary ones, characterized by the capillary number Ca = μ_{d}v/γ) modifies the pattern depending on the fluids viscosity ratio, M = μ_{d}/μ_{i}, towards (i) viscous fingering (VF) for an unfavorable ratio, M > 1, or (ii) compact (CO) for a favorable ratio (M < 1)^{8,9}. Here μ is the viscosity, v is the characteristic fluid velocity, and γ is the interfacial tension, where subscripts d and i denote defending and invading, respectively.
Another important property is wettability, namely the relative affinity of the fluids to the solid. Increasing affinity of the invading fluid (from drainage to imbibition, when the invading fluid is more wetting) smoothes the invasion front, even at high, unfavorable M^{10}. At low rates, increasing wettability leads to a transition between CF and CO, whereas increasing Ca enhances viscous instabilities promoting VF, regardless of wettability^{11,12}. We note that the frequent use of the term “(in)stability” to describe the pattern, and the interchange of “stability” with “efficiency” or “compactness”. To avoid confusion between patterns (e.g. VF) and underlying mechanisms (e.g. hydrodynamic instabilities), we use “compact”, “efficient” or “stable pattern”.
Experimental and computational capabilities limit the number of mechanisms that can be modeled. Here, we focus on the following subset: capillarity, viscosity, wettability, and their coupling with random disorder in pore and/or particle sizes. We exclude here gravity and buoyancy effects. We also focus on size disorder alone, excluding other types of heterogeneity including in wetting properties^{13} or with spatial correlations such as layers or dual porosity media^{14,15}.
Current understanding of disorder effects
Disorder in pore sizes is inherent in natural media such as soils and rocks^{4}, and, to some extent, even in engineered devices due to limited fabrication resolution^{16}. In some industrial applications, where homogenous fluid distribution and control over resulting patterns are key, low disorder is crucial and highly desirable^{17}. We note that disorder as well as preferential pathways and heterogenous fluid distributions can be advantageous in applications where fluid mixing and reactions^{6,7} are needed, and undesirable when efficient sweep of hydrocarbons^{5} or contaminants^{6} are crucial. As summarized below, while the importance of disorder is widelyrecognized, a systematic exploration including quantitative analysis of samples of different, known disorder at variable wettability and rates is lacking.
The effect of disorder on the invasion morphology when either capillary or viscous forces are dominant seems to be univocally accepted. For slow drainage, high disorder was shown to promote trapping, leading to a transition from CO to CF^{18,19,20,21,22,23,24}. For slow imbibition, quasistatic simulations show a transition from compact to faceted (FA) growth as disorder is decreased^{20,25}. Ordered FA patterns were also observed experimentally, for imbibition in ordered samples (uniform pore sizes) at favorable M^{9}. An interesting correlation between fluid invasion and magnetic systems was drawn regarding the interplay between disorder and the smoothing (“stabilizing”) action of cooperative events^{26}. At the other extremity of high Ca (VF regime), decreasing disorder produces snowflakelike patterns^{22,27} with fewer, less tortuous fingers (“ordered dendritic”, OD). We stress that FA and OD are only obtained for samples with nearlyuniform pore sizes, here resulting from uniformly sized particles ordered on a lattice. Such patterns would not appear in granular materials (including monosized bead packs) due to the large variability in apertures provided by packing disorder.
At intermediate Ca where both viscosity and capillarity are important, the qualitative paradigm (“conventional wisdom”^{24}) is that lowering disorder enhances the displacement efficiency^{18,21,22,23,24}. Few works derived a modified capillary number, Ca^{*}, which includes the impact of disorder via the width of the capillary thresholds, neglecting its effect on the viscous forces. Quantitatively, this implies an inverse relationship between Ca^{*} and disorder, namely that increasing disorder (at a given rate, Ca) produces a more CFlike pattern, increasing the transitional Ca between CF to VF, Ca_{CF/VF}^{18,21,22,23,24}. We point to a subtle yet crucial inconsistency in the above: if increasing disorder increases Ca_{CF/VF}, promoting a more CFlike pattern, sweep efficiency should increase (since VF is much less efficient that CF^{18,21,22,23,24,28}), contrasting the observations stated above.
Here, we address this problematic paradigm via a combination of porescale simulations, micromodel experiments and scaling analysis. To the best of our knowledge, our study is the first systematic, quantitative investigation of the impact of disorder and its coupling with rates and wettability. Our findings improve our understanding, generalizing the phase diagram of fluid invasion including rates, viscosity ratio, buoyancy and wettability effects^{8,11,12,28} by adding an additional axis–disorder.
Results
Problem setting and methodology
We consider radial displacement of a viscous fluid by an inviscid fluid (high, unfavorable ratio M) at a fixed rate Q in samples of different disorder in particle sizes. Details of the simulations and experiments are provided in Methods and Supplementary Material. Briefly, our 2D medium is made of “particles” (cylindrical pillars) of diameters d drawn from a uniform distribution of width λ, , providing welldefined pores and throats (of size r, with a triangular distribution), see Fig. 1a–c. Experimentally, we use a plastic micromodel initially saturated with glycerol, withdrawn from the cell’s perimeter (outlet), allowing air to invade at its center. Timelapse photography provides the pattern evolution (Fig. 1f). The large data set required for the quantitative analysis, including 240 runs on samples of different disorder, at various rates and wetting properties, was generated numerically, with the porescale model of Holtzman and Segre^{12}.
Simulated patterns
Our simulations capture the plethora of invasion behaviors and emergent patterns as the disorder, rate and wettability are varied. For high disorder (λ = 0.82), we reproduce the transition from CF to VF as the rate increases in drainage^{8} (wetting angle θ < 90°, θ measured through the defending fluid, see Fig. 1c), and the smoothing (“stabilizing”) effect of increasing θ towards imbibition (θ > 90°), reducing trapping^{11,12} (Fig. 2). We show that lowering the disorder λ enhances the displacement efficiency, by inhibiting trapping and formation of thin, tortuous fingers at low and high rates, respectively. While in highlydisordered systems the pattern is random (showing no dependence on the underlying structured lattice), reducing λ amplifies the impact of the underlying lattice, suppressing both trapping and fingering, eventually resulting in the following transitions: (i) from CF to CO in slow drainage^{11}; (ii) from CO to FA in slow imbibition^{25}; and (iii) from VF to OD^{22,27} at high rates. We point that compact displacement is obtained despite of the highly unfavorable viscosity ratio, M = μ_{d}/μ_{i} ≈ 55. Reducing λ also suppresses the impact of wettability; that is, the competing effects of reducing λ and increasing θ offset each other (Fig. 2).
Experimental validation
To validate our numerical findings, we conducted micromodel experiments with two cells of different disorder (λ = 0.22 and 0.52) of geometry identical to the simulations, displacing glycerol by air (μ_{d} ≈ 1 Pa · s, μ_{i} = 1.8 · 10^{−5} Pa · s, γ ≈ 6.3 · 10^{−2} N/m, θ = 75° ± 5°, see Methods). The experimental patterns support our findings that reducing λ enhances the displacement efficiency by (i) suppressing trapping at low Ca, leading to a transition from CF to CO; and (ii) reducing the number of tortuous fingers, increasing their width (from VF to OD) at high Ca (Fig. 3). The experiments also show the impact of λ on the invasion dynamics: (i) the transition in the mode of front propagation from radiallysymmetric and continuous (CO) to intermittent and asymmetrical (CF) as λ is increased at low rates (Videos 1 and 2 in the the supplementary material); and (ii) radial growth of viscous fingers with vanishing impact of the underlying lattice as λ increases (from OD to VF, see Videos 3 and 4) at high rates.
We note that while patterns in simulations and experiments are similar in type (e.g. number and width of fingers or interface roughness), they are not identical. Potential causes for this mismatch include (1) manufacturing defects in pillar placement and shape (Fig. 1f, insets) and (2) mechanisms not included in our model such as snapoff^{9,29} or droplet fragmentation^{30} in lowporosity rocks, and thin wetting fluid films progressing ahead of the main imbibition front^{31}. Manufacturing errors could greatly affect the pattern due to its sensitivity to small geometrical details; e.g. enlarging a single aperture can allow invasion of multiple pores, otherwise inaccessible. In contrast, for the current settings of relatively high viscosity contrast M, low contact angle (vs. 150° in ref. 31), high porosity and small throat to pore size ratio, the aforementioned mechanisms should not be dominant^{9,29}. A more conclusive validation requires improved manufacturing accuracy as well as a more rigorous, quantitative analysis. Such experiments are underway. Modeling mechanisms such as droplet fragmentation or film flow is a challenge which is outside the scope of this paper^{3,4,29}, however of great interest for future research.
Pattern characteristics
We characterize the patterns through their finger width w, interfacial areas A_{inter} and A_{front}, and breakthrough saturation S. The interfacial areas (lengths in 2D) are computed from the ratio of interfacial and invaded pores, including trapped regions (A_{inter}) or excluding them (A_{front}). The areas are normalized by the invaded volume V_{inv} (area in 2D), and multiplied by the lattice spacing a to make them dimensionless. The finger width w is evaluated by skeletonizing the pattern with a Voronoi algorithm, and measuring the distance (in lattice units a) of the medial line from the interface. In evaluating w we include small clusters trapped within fingers, unlike some previous studies where these were ignored^{28} (resulting in larger w).
Our simulations point to the persistent effect (across variable Ca and θ) of increasing disorder λ, manifested as an increase in A_{inter} and A_{front} (approaching the theoretical limit of 1 for VF at high rates), and a decrease in w (Fig. 4a–c). The counteracting effects of increasing θ and lowering λ are demonstrated by a nearlyconstant, low A_{inter} and A_{front} and high w for λ < 0.6, in particular at low Ca (approaching the limit a/L for CO), see Fig. 4d–f. As shown below, this insensitivity is caused by two competing effects of decreasing λ in imbibition (high θ): (i) reducing the variation in capillary thresholds, increasing compactness; and (ii) inhibiting cooperative events which smooth the interface, hence decreasing compactness.
Invasion selectivity and cooperativity
To further explain the coupling between disorder, rate and wettability, we define two characteristics: invasion selectivity and cooperativity. Selectivity, evaluated here from the mean invaded throat size , increases with λ and Ca, while decreasing with θ to a minimum at slow imbibition (Fig. 5a). Reduced selectivity implies greater dependency of the invasion pattern on the underlying pore geometry (e.g. FA and OD in Fig. 2). This occurs in ordered systems (λ = 0.22), where the radiallysymmetric invasion (Video 1 in supplementary material) samples nearlyequally all throat sizes (retaining the triangular distribution, Fig. 5c) such that the mean invaded size is close to the mean ( = 0.54a). In contrast, high disorder provides constrictions with high entry pressures that remain noninvaded (Video 2 in supplementary material), leading to a skewed distribution with a larger mean . Such high selectivity is mostly pronounced at slow drainage, where small pores are completely avoided (Fig. 5a–b). In imbibition, since cooperative invasion occurs at lower capillary pressures than burst instabilities^{12}, smaller pores can be invaded than in drainage, reducing .
Cooperativity ε_{coop} is the relative number of nonlocal, cooperative pore filling events (overlaps). Overlaps, which increase in occurrence with θ (and do not appear below ~60°), stabilize imbibition patterns by suppressing fingering and trapping^{12}. Schematic side panels in Fig. 6 show two pairs of adjacent menisci at a similar curvature for λ = 0.82 and 0.22, demonstrate that poresize homogeneity hinders overlaps. Since disorder also promotes trapping, the two effects counteract, leading to the small sensitivity to λ in slow imbibition; this is particularly noticeable for A_{front}, which is more affected by trapping than A_{inter} or w (Fig. 4d–f). Increasing rates diminishes both selectivity and cooperativity, as pressure screening results in thin fingers invading only into more permeable regions^{12} (Figs 5 and 6). Consequently, the mechanism for invasion selectivity changes with rates: at low Ca it is the high capillary thresholds along the interface (locally), whereas at high Ca the flow resistance–a nonlocal effect which depends on the connectivity of larger pores–becomes dominant.
Trapping and sweep efficiency
One of the most important characteristics of fluid displacement from a practical standpoint–describing the ability to produce oil or water and displace a contaminant–is the sweep efficiency. Sweep is intimately related to trapping, leaving behind isolated patches of the defending fluid. We define sweep S and trapping fraction χ_{trap} from the following dimensionless volumetric ratios: S = V_{inv}/V_{tot}, where V_{tot} is the volume of the convex polygon wrapping the pattern (Fig. 7a, inset), and χ_{trap} = V_{trap}/V_{inv}, where V_{trap} is the volume of trapped fluid (Fig. 7c–f, in red).
The complex interplay between disorder, wettability and rates is demonstrated by the nonlinear, nonmonotonic behavior of sweep and trapping^{32}. Both lowering disorder λ and increasing wetting angle θ provide a similar effect: suppressing trapping hence increasing sweep, to almost 100% at low rates (Fig. 7a–b). Flow rate strongly impacts both S and χ_{trap}. In slow drainage (low Ca and θ) and high λ, the patchy CFlike pattern traps a significant portion of the defending fluid (Fig. 7b; see pattern in Fig. 7c). At slow imbibition (high θ), lowering disorder inhibits both cooperative pore filling (Fig. 6) and trapping, effects which offset each other, explaining the observed minimal impact of λ (cf. Fig. 4d–f). Increasing the rate promotes viscous instabilities and invasion by thin fingers which leave most of the defending fluid behind (Fig. 7f), minimizing sweep despite of the reduced trapping. Rates change not only the trapped volume, but also the underlying mechanism: from multiple patches within thick fingers (CF) at low Ca (Fig. 7c–d) to fewer patches trapped between thin fingers (VF) at high Ca (Fig. 7f).
Scaling analysis: Introducing disorder effects
In light of the complex effect of disorder, and, in particular, the ambiguity in the literature regarding its interplay with viscous forces, we address this analytically via scaling, deriving a disorderdependent number Ca*. We begin with the classical definition, Ca = δp_{vis}/δp_{cap}, where δp_{vis} and δp_{cap} are the characteristic viscous and capillary forces^{9}. The force driving the growth of individual fingers perpendicular to the interface (along the direction of the externallyapplied pressure drop) δp_{vis} is evaluated from the pressure drop in the viscous defending fluid over a characteristic length L_{vis}, δp_{vis} ~ ∇p_{vis}L_{vis}. Here ∇p_{vis} ~ μ_{d}v/k is the gradient and k is the medium’s permeability. The capillary force is evaluated from a characteristic entry pressure, δp_{cap} ~ γ/r_{c}, where r_{c} is a characteristic aperture, providing^{33}
The classical expression^{9} Ca = μ_{d}v/γ is obtained by evaluating δp_{vis} at the porescale, , together with the simplifying assumptions and .
Here, we point to an inherent shortcoming in the above definition when disorder is introduced: the assumption ignores the effect of interpore connectivity, which controls the resistance to viscous pressure dissipation (flow). We claim that disorder in pore throat sizes λ affects both (i) capillary forces δp_{cap} through the entry threshold distribution which controls the invasion order along the interface (locally), as well as (ii) viscous forces through the permeability k, a nonlocal effect, not accounted for in previous works^{18,21,22,23,24}. To include the latter in our definition of Ca*, we evaluate k as an effective permeability: considering finger growth in the radial direction, we use the weighted harmonic mean of the local (interpore) permeabilities (i.e. resistors in series), , providing
The main outcome of Eq. (2) is that since increasing disorder (the width of r distribution) decreases the size of the smallest throats (“bottlenecks”) and thus the permeability k (which is biased towards the smallest r values), it increases δp_{vis}. If the accompanying increase in δp_{cap} is smaller, this would amount to increasing Ca*.
In our derivation, unlike the classical one presented above, the terms r_{c} and in Eq. (2) represent different characteristic lengths (though both at the porescale), hence are not equal: r_{c} arises from the characteristic threshold, δp_{cap} ~ γ/r_{c}, whereas is our choice for the pore scale characteristic length for pressure dissipation, . Furthermore, the choice of r_{c} in Eq. (2) depends on wettability. In drainage, since invasion occurs mostly though burst instabilities^{12} which strongly depend on throat sizes r, the distribution is dominant; thus, we evaluate r_{c} using the standard deviation, r_{c} = σ(r). In imbibition, the increasing occurrence of overlaps with λ (Fig. 6) makes for a complex dependence of the characteristic invaded size r_{c} on disorder. Since predicting this dependence is out of the scope of this paper, we simply use for imbibition.
As samples with higher λ exhibit more tortuous, thinner fingers (at a given Ca, see insets in Fig. 8), plotting the pattern characteristic A_{inter} vs. our rescaled Ca^{*} partially collapses curves of different λ, (Fig. 8; similar collapse observed for A_{front} and w). This indicates a direct relationship between Ca* and λ (Fig. 8b, lower inset), namely a lower transitional Ca_{CF/VF} value at higher λ, in par with the inverse relationship (and increase in Ca_{CF/VF}) in the literature^{18,21,22,23,24}. Our scaling analysis also quantifies the decreased sensitivity of the emergent pattern to λ as the wetting angle θ increases (highlighted in Fig. 4d–f): Ca*/Ca is ~10 times larger for λ = 0.82 than for λ = 0.22 for drainage (θ = 5°), vs. only ~2.5 for imbibition (θ = 120°), see inset in Fig. 8b. We note that while our scaling is a valuable quantitative explanation of our findings, the expression in Eq. (2) and consequent values (Fig. 8) were derived for our 2D medium with uniform distribution of round particles; extension to other types of media is of interest for future research.
Discussion
We study the impact of random pore size disorder on the fluidfluid displacement in porous media. We use a novel porescale model which provides a mechanistic description of both drainage and imbibition. Our numerical results are validated against micromodel experiments, and explained theoretically by scaling analysis. To the best of our knowledge this is the first systematic, quantitative study of the impact of disorder and its interplay with flow rates and wettability.
We show that lowering disorder λ increases the pattern compactness, with a smoother fluidfluid interface. We demonstrate that the effect of disorder depends on its coupling with flow rate and wettability: (i) at low rates, a more pronounced impact of λ on capillary thresholds and hence on the order of invasion and trapping; (ii) at high rates, increasing λ strongly increases the viscous pressure drop by decreasing pore connectivity, promoting pressure screening and viscous instabilities, increasing the number of thin, tortuous fingers; and (iii) increasing the wetting angle θ stabilizes the invasion pattern by reducing trapping and smoothing the interface, thus minimizing the impact of disorder. At low λ, the underlying pore geometry (lattice structure) becomes dominant, in particular in imbibition, leading to symmetrical growth of faceted, compact pattern at low Ca and dendritic fingers at high Ca.
While our observation that decreasing disorder increases the sweep efficiency agrees with previous studies^{18,20,21,22,23,24,25,27}, our interpretation does not: we emphasize the previously ignored impact of porescale disorder on the effective, samplescale connectivity (permeability), and thus on the viscous forces. We quantify this effect by deriving a disorderdependent capillary number Ca^{*} providing a direct relationship between Ca^{*} and λ, that is a lower transitional Ca_{CF/VF} value at higher λ, in par with previous works^{18,21,22,23,24}. Our findings delineate the complex interplay among disorder, rates and wettability, via a simplified 2D model. Valuable future work includes generalization of the model towards 3D granular pack with correlated heterogeneities (more representative of soils and rocks), inclusion of additional mechanisms such as droplet fragmentation or film flow, and a more rigorous experimental validation by improving manufacturing accuracy and quantitative analysis.
In summary, our work offers a fresh perspective into a longstanding paradigm of significance in processes where efficiency of fluid extraction/injection and mixing and reaction of the fluids are crucial. Increasing disorder promotes fingering, which limits the recovery of subsurface fluids such as hydrocarbons^{5} or contaminants^{6}, while increasing interfacial areas which controls fluid mixing and reactions^{34} in microfluidics^{16,17}, subsurface remediation^{6}, soil aeration^{35}, and longterm CO_{2} geosequestration by carbonate mineralization^{7}.
Methods
Model medium: 2D analog
The main objective of this work is to gain fundamental understanding of the complex interactions among disorder, wettability and rates. Therefore, we choose the simplest representation (for both numerics and experiments) of a partiallywettable, disordered porous medium that retains the most crucial aspects of the behavior of such medium. We consider here the following model system: cylindrical solid pillars placed on a regular lattice (Fig. 1), noting that consideration of the convoluted 3D pore geometry (relevant for instance to natural sediments) would hinder basic insights, and thus should be left to a later stage. We introduce disorder through variations in particle sizes, rather than through randomness in particle positions or in the coordination number of pores, since the former allows a more rigorous quantitative comparison among different samples. Similarly, our choice of triangular lattice limits the number of menisci which can invade into a pore simultaneously to two, retaining the crucial aspect of cooperative pore filling while avoiding the ambiguity of resolving a burst on a square lattice^{20}.
We construct squareshaped samples of size L = N_{x}a by placing N_{x} × N_{y} particles (N_{y} × 2N_{x} pores), where and a is the lattice spacing. Each particle triplet defines a pore with volume V connected to three neighboring pores by throats with aperture 0 < r ≲ a; to avoid closed throats due to particle overlap we enforce , see Fig. 1c. Pillar diameters are much smaller than their height, d ≪ h, such that the inplane curvature is much larger than the outofplane curvature, R_{in} ≪ R_{out}. This allows us to approximate the meniscus as 2D, with a radius of curvature .
Numerical simulations
Simulations are conducted with the model of Holtzman and Segre^{12}, summarized below (see supplementary material for further details). This model can accommodate a wide range of properties and conditions including flow rates, wetting properties and viscosities. To the best of our knowledge, it is the only porescale model which provides a mechanistic description of the dynamics of partiallywetting invasion in a large, disordered domain. Previous models were limited by computational costs^{3,4,29}, compromising the dynamics by assuming quasistatic displacement^{19,20} or the size and heterogeneity of the domain^{24,32}.
We represent the fluidfluid interface as a sequence of menisci, where each meniscus is a circular arcs which intersects a pair of particles at the prescribed contact angle θ, and has a radius of curvature R = γ/Δp according to the YoungLaplace law. Here Δp is the pressure jump across the meniscus. The angle θ is measured through the defending fluid (i.e. θ < 90° for drainage), and represents an effective advancing angle, which includes dynamic effects^{3}. Knowledge of R and θ allows to resolve analytically the position and hence stability of each meniscus.
A crucial feature of our model is its account for cooperative porefilling (overlaps^{20}), which become dominant at high θ. Overlap is a nonlocal mechanism as it is affected by menisci in multiple pores, acting to smooth the interface^{12,20}. Menisci are tested for three types of capillary instabilities^{20}: (1) Haines jump or burst, when the curvature exceeds a threshold set by the local geometry; (2) touch, when a meniscus intersects a third, downstream particle; and (3) overlap of adjacent menisci, destabilizing each other [Fig. 1(c–e)]. Once destabilized, the meniscus incipiently invades the downstream pore, at a rate evaluated from the fluid’s viscous resistance (see supplementary material for details). The finite pore filling time in our model captures the invasion dynamics, including the spatiotemporal nonlocality associated with rapid interfacial jumps and the consequent interface readjustments and pressure screening^{33,36}, overcoming a longstanding computational challenge^{3,29}.
Experimental setup
Micromodels allow visualization of the solids and fluids, making them a highly useful tool to study fluid displacement. Here, we use 3D printing (“stereolithography”), an additive method fabricating freeform solids using a computeraided design (CAD) file. A ProJet 3500 Multi Jet Printer (3D Systems Inc.) with “VisiJet M3 Crystal” plastic provided inplane and outofplane resolution of 50 and 32 μm, respectively^{37}. The limited resolution resulted in rough, nonround pillars, and, though rare, a few that are misplaced (offlattice), see insets in Fig. 1f. We fabricated two cells of geometry similar to the numerical samples (L = 100a) with λ = 0.22 and 0.52, however with lattice spacing a = 1 mm (vs. 0.5 mm in simulations). Pillar height of h = 3 mm was chosen to ensure sufficiently large aspect ratio h/r such that the meniscus can be approximated as 2D, while small enough to minimize hydrostatic pressure and thus 3D, outofplane effects inducing vertical flows. The lattice is embedded in a frame with a trench (of width 1 cm) around it to ensure evenly distributed withdrawal. The chip is sandwiched between two 1 cmthick acrylic plates, with an outlet crosssectional area A_{out} ≈ 5.5 · 10^{−4} m^{2}.
The cell is initially filled with glycerol (~99.5% purity with μ_{d} ≈ 1 Pa · s and γ ≈ 6.3 · 10^{−2} N/m at ~25 °C, Gadot Chemical Terminals LTD.). A highviscosity fluid was selected to probe high Ca, where the CF–VF transition occurs. The contact angle (for both acrylic and VisiJet M3 Crystal) was measured to be 75° ± 5° using a sessile drop goniometer (EasyDrop DSA20E, Krüss GmbH). Glycerol is withdrawn from ports at the cell corners by a syringe pump (Harvard Apparatus PHD ULTRA 703007) at a fixed rate Q, letting air (μ_{i} = 1.8 · 10^{−5} Pa · s) invade freely through a central inlet (Fig. 1f). Ca values in Fig. 3 correspond to Q = 0.2, 0.5, 2, 5, 20, 50 and 100 ml/min. The cell is held horizontally to avoid gravity effects. The pattern evolution is tracked by timelapse photography using a CMOS camera (uEye 3520, IDS 1.3 MP). We illuminate the cell from above with LEDs. To improve image contrast, the bottom acrylic plate was painted black, and the inner side of the top plate was sandpapered, causing dry areas to appear opaque.
Additional Information
How to cite this article: Holtzman, R. Effects of PoreScale Disorder on Fluid Displacement in PartiallyWettable Porous Media. Sci. Rep. 6, 36221; doi: 10.1038/srep36221 (2016).
Publisher’s note: Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
References
Sahimi, M. Flow and transport in porous media and fractured rock (WileyVCH, 2011) 2 edn.
Pelcé, P. New visions on form and growth (Oxford University, New York, 2004).
Meakin, P. & Tartakovsky, A. M. Modeling and simulation of porescale multiphase fluid flow and reactive transport in fractured and porous media. Rev. Geophys. 47, RG3002 (2009).
Bultreys, T., De Boever, W. & Cnudde, V. Imaging and imagebased fluid transport modeling at the pore scale in geological materials: A practical introduction to the current stateoftheart. EarthScience Rev. 155, 93–128 (2016).
Lake, L. W., Johns, R., Rossen, B. & Pope, G. Fundamentals of Enhanced Oil Recovery (Society of Petroleum Engineers, 2014).
Nadim, F., Hoag, G. E., Liu, S., Carley, R. J. & Zack, P. Detection and remediation of soil and aquifer systems contaminated with petroleum products: An overview. J Petrol. Sci. Eng. 26, 169–178 (2000).
Matter, J. M. et al. Rapid carbon mineralization for permanent disposal of anthropogenic carbon dioxide emissions. Science 352, 1312–1314 (2016).
Lenormand, R., Touboul, E. & Zarcone, C. Numerical models and experiments on immiscible displacements in porous media. J. Fluid Mech. 189, 165–187 (1988).
Lenormand, R. Liquids in porous media. J. Phys. Condens. Matter 2, SA79–SA88 (1990).
Stokes, J. P. et al. Interfacial stability of immiscible displacement in a porous medium. Phys. Rev. Lett. 57, 1718–1721 (1986).
Trojer, M., Szulczewski, M. L. & Juanes, R. Stabilizing fluidfluid displacements in porous media through wettability alteration. Phys. Rev. Appl. 3, 054008 (2015).
Holtzman, R. & Segre, E. Wettability stabilizes fluid invasion into porous media via nonlocal, cooperative pore filling. Phys. Rev. Lett. 115, 164501 (2015).
Murison, J. et al. Wetting heterogeneities in porous media control flow dissipation. Phys. Rev. Appl. 2, 034002 (2014).
Zhang, C., Oostrom, M., Grate, J. W., Wietsma, T. W. & Warner, M. G. Liquid CO2 displacement of water in a dualpermeability pore network micromodel. Environ. Sci. Technol. 45, 7581–7588 (2011).
Akhlaghi Amiri, H. A. & Hamouda, A. A. Porescale modeling of nonisothermal two phase flow in 2D porous media: Influences of viscosity, capillarity, wettability and heterogeneity. Int. J. Multiph. Flow 61, 14–27 (2014).
Stone, H. A., Stroock, A. D. & Ajdari, A. Engineering flows in small devices. Annu. Rev. Fluid Mech. 36, 381–411 (2004).
Kim, H., Zheng, Z. & Stone, H. A. Noncircular stable displacement patterns in a meshed porous layer. Langmuir 31, 5684–5688 (2015).
Yortsos, Y. C., Xu, B. & Salin, D. Phase diagram of fullydeveloped drainage in porous media. Phys. Rev. Lett. 79, 4581–4584 (1997).
Cieplak, M. & Robbins, M. O. Dynamical transition in quasistatic fluid invasion of porous media. Phys. Rev. Lett. 60, 2042–2045 (1998).
Cieplak, M. & Robbins, M. O. Influence of contact angle on quasistatic fluid invasion of porous media. Phys. Rev. B 41, 11508–11521 (1990).
Toussaint, R., Løvoll, G., Méheust, Y., Måløy, K. J. & Schmittbuhl, J. Influence of porescale disorder on viscous fingering during drainage. Europhys. Lett. 71, 583–589 (2005).
Holtzman, R. & Juanes, R. Crossover from fingering to fracturing in deformable disordered media. Phys. Rev. E 82, 046305 (2010).
Xu, W., Ok, J. T., Xiao, F., Neeves, K. B. & Yin, X. Effect of pore geometry and interfacial tension on wateroil displacement efficiency in oilwet microfluidic porous media analogs. Phys. Fluids 26, 093102 (2014).
Liu, H., Zhang, Y. & Valocchi, A. J. Lattice Boltzmann simulation of immiscible fluid displacement in porous media: Homogeneous versus heterogeneous pore network. Phys. Fluids 27, 052103 (2015).
Martys, N., Robbins, M. O. & Cieplak, M. Scaling relations for interface motion through disordered media: Application to twodimensional fluid invasion. Phys. Rev. B 44, 294–306 (1991).
Martys, N., Cieplak, M. & Robbins, M. O. Critical phenomena in fluid invasion of porous media. Phys. Rev. Lett. 66, 1058–1061 (1991).
Chen, J.D. & Wilkinson, D. Porescale viscous fingering in porous media. Phys. Rev. Lett. 55, 1892–1895 (1985).
Toussaint, R. et al. Twophase flow: Structure, upscaling, and consequences for macroscopic transport properties. Vadose Zo. J 11 (2012).
JoekarNiasar, V. & Hassanizadeh, S. M. Analysis of fundamentals of twophase flow in porous media using dynamic porenetwork models: A review. Crit. Rev. Environ. Sci. Technol. 42, 1895–1976 (2012).
Pak, T., Butler, I. B., Geiger, S., van Dijke, M. I. J. & Sorbie, K. S. Droplet fragmentation: 3D imaging of a previously unidentified porescale process during multiphase flow in porous media. Proc. Natl. Acad. Sci. 112, 1947–1952 (2015).
Zhao, B., MacMinn, C. W. & Juanes, R. Wettability control on multiphase flow in patterned microfluidics. Proc. Natl. Acad. Sci. 113, 10251–10256 (2016).
Liu, H., Valocchi, A. J., Kang, Q. & Werth, C. Porescale simulations of gas displacing liquid in a homogeneous pore network using the Lattice Boltzmann method. Transp. Porous Media 99, 555–580 (2013).
Løvoll, G., Méheust, Y., Toussaint, R., Schmittbuhl, J. & Måløy, K. J. Growth activity during fingering in a porous HeleShaw cell. Phys. Rev. E 70, 026301 (2004).
Jha, B., CuetoFelgueroso, L. & Juanes, R. Fluid mixing from viscous fingering. Phys. Rev. Lett. 106, 194502 (2011).
Li, Y., Jia, Z., Niu, W., Wang, J. & Zhang, M. Effect of postinfiltration soil aeration at different growth stages on growth and fruit quality of dripirrigated potted tomato plants Solanum lycopersicum. PLoS ONE 10, 1–16 (2015).
Armstrong, R. T. & Berg, S. Interfacial velocities and capillary pressure gradients during haines jumps. Phys. Rev. E 88, 043010 (2013).
Snyder, T. J. et al. 3D Systems’ technology overview and new applications in manufacturing, engineering, science, and education. 3D Print. Addit. Manuf. 1, 169–176 (2014).
Acknowledgements
The author thanks E. Segre and A. Naftali for invaluable assistance with the simulations (E.S. and A.N.) and experiments (E.S.). Financial support by the Israeli Science Foundation (#ISF867/13), the United StatesIsrael Binational Science Foundation (#BSF2012140) and the Israel Ministry of Agriculture and Rural Development (#821013713) is gratefully acknowledged.
Author information
Authors and Affiliations
Contributions
R.H. conceived the study, acquired the data, analyzed the results and wrote the manuscript.
Ethics declarations
Competing interests
The author declares no competing financial interests.
Electronic supplementary material
Rights and permissions
This work is licensed under a Creative Commons Attribution 4.0 International License. The images or other third party material in this article are included in the article’s Creative Commons license, unless indicated otherwise in the credit line; if the material is not included under the Creative Commons license, users will need to obtain permission from the license holder to reproduce the material. To view a copy of this license, visit http://creativecommons.org/licenses/by/4.0/
About this article
Cite this article
Holtzman, R. Effects of PoreScale Disorder on Fluid Displacement in PartiallyWettable Porous Media. Sci Rep 6, 36221 (2016). https://doi.org/10.1038/srep36221
Received:
Accepted:
Published:
DOI: https://doi.org/10.1038/srep36221
This article is cited by

Development of a novel experimental technique for the measurement of residual wall layer thickness in wateroil displacement flows
Scientific Reports (2023)

A Numerical Investigation on Effective Diffusion in CementBased Composites: The Role of Aggregate Shape
Transport in Porous Media (2022)

Porescale effects during the transition from capillary to viscositydominated flow dynamics within microfluidic porouslike domains
Scientific Reports (2021)

Understanding the role of wettability distribution on porefilling and displacement patterns in a homogeneous structure via quasi 3D porescale modelling
Scientific Reports (2021)

A Comprehensive Experimental Study on Immiscible Displacements in Porous Media: Effects of Capillary Forces, Viscous Forces, Wettability and Pore Geometries
Journal of Thermal Science (2021)
Comments
By submitting a comment you agree to abide by our Terms and Community Guidelines. If you find something abusive or that does not comply with our terms or guidelines please flag it as inappropriate.