Journal of Contaminant Hydrology 74 (2004) 61 – 81 www.elsevier.com/locate/jconhyd Secondary imbibition in NAPL-invaded mixed-wet sediments Ahmed Al-Futaisi a,b, Tad W. Patzek b,* a The Civil Engineering Department, Sultan Qaboos University, Oman, Saudi Arabia b Department of Civil and Environmental Engineering, Berkeley, CA 94720, USA Received 12 February 2003; received in revised form 16 January 2004; accepted 9 February 2004 Abstract A previously developed pore network model is used here to study the spontaneous and forced secondary imbibition of a NAPL-invaded sediment, as in the displacement of NAPL by waterflooding a mixed-wet soil. We use a 3D disordered pore network with a realistic representation of pore geometry and connectivity, and a quasi-static displacement model that fully describes the pore-scale physics. After primary drainage (NAPL displacing water) up to a maximum capillary pressure, we simulate secondary imbibition (water displacing NAPL). We conduct a parametric study of imbibition by varying systematically the controlling parameters: the advancing contact angles, the fraction of NAPL-wet pores, the interfacial tension, and the initial water saturation. Once the secondary imbibition is completed, the controlling displacement mechanisms, capillary pressures, relative permeabilities, and trapped NAPL saturations are reported. It is assumed that NAPL migrates into an initially strongly water-wet sediment, i.e., the receding contact angles are very small. However, depending on the surface mineralogy and chemical compositions of the immiscible fluid phases, the wettability of pore interiors is altered while the neighborhoods of pore corners remain strongly water-wet-resulting in a mixed-wet sediment. Here, we compare three different levels of wettability alteration: water-wet (advancing contact angles (20j to 55j), intermediate-wet (55j to 120j), and NAPL-wet (120j to 155j). The range of advancing contact angles and the fraction of NAPL-wet pores have dramatic effects on the NAPL-water capillary pressures and relative permeabilities. The spatially inhomogeneous interfacial tension has a minor impact on the trapped NAPL saturation and relative permeability to NAPL, and a slight effect on the relative permeability to water. The initial water saturation has a slight effect on the two-phase flow characteristics of water-wet sediments; however, with * Corresponding author. University of California, Department of Civil and Environmental Engineering, 437 Davis Hall, Berkely, CA 94720, USA. E-mail addresses: [email protected] (A. Al-Futaisi), [email protected] (T.W. Patzek). 0169-7722/$ - see front matter D 2004 Elsevier B.V. All rights reserved. doi:10.1016/j.jconhyd.2004.02.005 62 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 more NAPL-wet pores in the sediment, it starts to have a profound effect on the water and NAPL relative permeabilities. D 2004 Elsevier B.V. All rights reserved. Keywords: Pore network; Mixed-wet; Relative permeability; Capillary pressure; Secondary imbibition; Initial water saturation; Trapping 1. Introduction Understanding NAPL migration in the air- and water-saturated zones is important in contamination management projects. The spatial distribution of sediment wettability and the extent of wettability alteration of individual pores influence the two-phase flow characteristics (Al-Futaisi and Patzek, 2003b; Blunt and Scher, 1995; Blunt, 1998, 2001; Bradford and Leij, 1995; Morrow et al., 1986; Piri and Blunt, 2002). Although most soils and rocks are naturally strongly water-wet, NAPL invasion may alter their wettability to intermediate-wet or NAPL-wet (Dekker and Ritsema, 1994; Dwarakanath et al., 2002; Powers et al., 1996; Villaume, 1985). In fact, changing the soil wettability has been proposed in remediation and contaminant migration control schemes through the emplacement of organic-wet zones, or with the in situ chemical reactions (Burris and Antworth, 1992; Hayworth and Burris, 1997; Xu and Boyd, 1995). The degree to which the sediment wettability is altered depends on its mineralogy (Anderson, 1986), surface roughness and charge (Hirasaki, 1991; Morrow, 1975), contaminant aging (Buckley et al., 1995; Freer et al., 2002; Powers and Tamblin, 1995), presence of organic acids and bases (Dubey and Doe, 1993; Powers and Tamblin, 1995; Thomas et al., 1993), chemical composition (Brown and Neustadter, 1980; Buckley and Liu, 1998; Murphy et al., 1992), and aqueous chemistry (Demond et al., 1994; Wang and Guidry, 1994; Zheng and Powers, 1999). With all of these variables that are difficult to quantify, the sediment wettability should be modeled as a spatially heterogeneous random variable. Solid wettability is heterogeneous macroscopically in the entire soil volume, and microscopically inside each pore. Those parts of the pore-wall surface that are exposed to by NAPL (usually the pore center) may have different wettability from those in contact with water (usually the pore corners). We then say that the soil is mixed-wet, as suggested by Salathiel (1973). In the petroleum literature, evidence points toward mixed-wettability as the most likely state of the majority of oil reservoirs. Salathiel reported experiments in which the initially water-saturated permeable rock was invaded with a crude oil, and the solid’s wettability was altered by adsorption of the crude oil components. He concluded that the parts of the rock surface in contact with connate water were protected from adsorption. Since then, efforts have been directed towards explaining physical and chemical aspects of mixed-wettability (Anderson, 1986; Buckley et al., 1995; Melrose, 1982; Morrow, 1990). Mixed-wettability can be broadly defined to include any degree of wetting alteration at the parts of the rock surface exposed to crude oil (Buckley et al., 1998). The rock wettability is altered following adsorption of asphaltenes or other surfaceactive compounds that essentially coat the mineral surface with an organic layer (Demond A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 63 et al., 1994; Kovscek et al., 1993; Powers and Tamblin, 1995; Zheng et al., 2001). In soils, one should expect a wider range of wettability alteration caused by the presence of complex organic and inorganic compounds, and high level of chemical and biological activity. Researchers differ as to how to induce or model a mixed-wet porous medium. Kovscek et al. (1993) were the first to propose a pore network model that produces mixed wettability. They suggested that the stability and thickness of water films between the oil and the solid surface determine wetting in oil/water/rock systems. When the water films rupture, the middle part of the pore wall becomes oil-wet, h = 180j, whereas the near-corner parts of the pore wall remain water-wet, h = 0j. The wettability alteration model by Kovscek et al. has been adopted in several pore-network models (Blunt, 1997, 1998, 2001; Dixit et al., 1999; Hui and Blunt, 2000a,b; Man and Jing, 1999; Piri and Blunt, 2002). The main difficulty of this approach is quantifying the disjoining pressure at which the water films rupture. How exactly a water film ruptures is less important than the altered value of advancing contact angle after the rupture. Dixit et al. (1999) represented their mixed-wet system using a pore network with different fractions of oilwet pores (big pores) and water-wet pores (small pores). Water displaces oil first from the water-wet pores and then from the oil-wet pores. Dixit et al. performed several simulations with different fractions of oil-wet pores. In their representation, each pore has a single wettability state but the rock wettability varies in space. Masalmeh (2002), in his laboratory experiments, let primary drainage establish the mixed-wet rock. He conducted primary drainage up to different values of maximum capillary pressure, Pmax c , i.e., each value of Pmax resulted in a rock with a different fraction of oil-wet pores. Then c the rock samples were aged for 4 weeks, and secondary imbibition was performed. This approach produces different mixed-wet rock samples. Finally, Bradford and Leij (1996) obtained their fractionally wet media by combining untreated and OTS-treated1 sand using 0%, 25%, 50%, 75% and 100% of OTS-treated sand. The untreated sands were strongly water-wet, while the OTS-treated sand was oil-wet. The two types of sand were then mixed in different proportions in a shaker for 5 h. Notice that this approach produces pores with different combinations of completely oil-wet walls and completely water-wet walls in a single pore.2 Despite all the progress to date, explaining and reproducing mixed-wettability remains a significant challenge. The objective of this paper is, first, to develop several realistic microscopic distributions of altered wettability of mixed-wet porous media. Then, we study secondary imbibition in these mixed-wet porous media. In our analysis, we adopt the Kovscek et al. (1993) framework with two major differences. First, we assume that during primary drainage some of the water films break at random for whatever reason.3 Second, the random advancing contact angles are not restricted to 0j 1 OTS is octadecyltrichlorosilane. Therefore, the porous media obtained by Bradford and Leij (1996) are not mixed-wet and do not reproduce the naturally altered rocks. 3 We argue that in drainage to a moderately high capillary pressure, the rupture disjoining pressure is commonly exceeded. We do not know what is the new advancing contact angle. 2 64 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 and 180j, but are allowed to vary with any value between 0j and 180j. The flow characteristics of the various secondary imbibition processes are calculated using our two-phase pore network model (Al-Futaisi and Patzek, 2003b; Patzek, 2001) which has been developed to account for any degree of wettability alteration. In a recent paper (AlFutaisi and Patzek, 2003b), this model has been used to study the effect of wettability alteration on the two-phase flow characteristics using very narrow ranges of advancing contact angles. In this paper we consider a wider range of advancing contact angles by focusing on three different types of wetting: water-wet (contact angles 20j to 55j), intermediate-wet (55j to 120j), and NAPL-wet (120j to 155j). We provide a detailed comparison among these three wettability ranges, and study the impact of the fraction of NAPL-wet pores, the inhomogeneous NAPL/water interfacial tension, and the initial water saturation. 2. Pore network model The network used in this analysis is a realistic representation of a sample of Bentheimer sandstone reconstructed from the 3D micro-focused X-ray CT image. The complex topology and geometry of the network is detailed in Øren et al. (1998), Patzek (2001). The two-phase flow model is quasi-static, i.e., capillary forces dominate, the effects of gravity are incorporated, and the effects of viscous forces are ignored. The flow simulations proceed in the following sequence: (1) fully saturate the network with water, (2) perform primary drainage (NAPL displaces water) up to a predefined maximum capillary pressure, (3) alter wettability, and (4) perform secondary imbibition (water displaces NAPL). The resulting capillary pressure curves are calculated using percolation algorithms (Al-Futaisi and Patzek, 2003b) with piston-type, snap-off, and cooperative pore-body filling mechanisms (Øren et al., 1998; Patzek, 2001). The relative permeabilities to water and NAPL are calculated using Darcy’s law and accurate expressions for the hydraulic conductances in bulk flow (Patzek and Silin, 2001), corner flow (Patzek and Kristensen, 2001), and intermediate-layer flow (Al-Futaisi and Patzek, 2003c). The spatial distribution of trapped NAPL clusters is determined using the Hoshen – Kopelman algorithm (Hoshen and Kopelman, 1976) extended by us to disordered networks (AlFutaisi and Patzek, 2003a). 3. Development of mixed-wettability A wettability alteration scenario that produces both water- and oil-wet regions in a single pore has been proposed by Kovscek et al. (1993), and has been used to compute the macroscopic capillary pressure curve for a bundle of star-shaped pores. Kovscek et al. argued that upon initial invasion of oil into a water-filled pore, thin water films separate the oil from the pore walls. The water films remain stable as long as the capillary pressure does not exceed the system-dependent rupture disjoining-pressure. As more oil is introduced into the reservoir, the oil –water capillary pressure increases, the rupture disjoining-pressure may be exceeded, and the water films may break. According A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 65 to Kovscek et al., where the thin water films break, the walls of the pores become strongly oil-wet (180j water advancing contact angle), whereas the water-filled corners of these pores remain strongly water-wet (the advancing contact angle and receding contact angle are both equal to 0j). Recently, Freer et al. (2002) provided a detailed discussion of deficiencies in the conceptual model of Kovscek et al. (1993). In particular, the assumption of zero receding contact angle and 180j advancing contact angle seems to be unrealistic. Based on the experiments with a crude oil droplet on mica, Freer et al. (2002) have postulated that following breakage of the thin water films, a range of receding and advancing contact angles is possible. This possible variability of receding and advancing contact angles results in a much richer behavior of secondary imbibition than that outlined by Kovscek et al. (1993). In this paper, we extend the Kovscek et al. scenario to any degree of wettability alteration (arbitrary values of contact angles), and study the ensuing NAPL/water flow characteristics during secondary imbibition. The important role of the water-receding and advancing contact angles, hr and ha, in drainage and imbibition of a single pore can be illustrated with the idealized cylindrical duct shown in Fig. 1. Initially, this duct is completely filled with water, and the solid walls are naturally water-wet, Fig. 1(a). Primary drainage starts by increasing capillary pressure, which allows the NAPL to migrate into the duct when the capillary entry pressure is exceeded. To avoid confusion in defining the wetting and nonwetting fluid phase, we define capillary pressure as the difference between the NAPL and water pressures: Pc :¼ PNAPL Pw ð1Þ The contact angles are always measured through water. When NAPL invades, it occupies the center of the duct, and water resides in the corners of the duct. After the NAPL recedes some distance toward the duct corners, the water films rupture and parts of the duct wall become NAPL-wet as indicated in Fig. 1(b) by the thick lines. It is usually assumed that the primary drainage receding contact angle is very small, around zero (Ma et al., 1996). However, Freer et al. (2002) suggest that, when appropriately measured with aged interfaces, water receding contact angles can reach much larger values (up to 50j). These large values of receding contact angle may have important implications on the NAPL/water configurations in the pores during primary drainage. For example, the corner water can now be completely displaced from the pore corners, Fig. 1. Possible two fluid configurations in a single pore: (a) an initially water-filled pore, (b) spontaneous imbibition, (c) force imbibition, (d) forced imbibition with NAPL layers (gray is water and white is NAPL). 66 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 and water trapping is possible. Until further experiments verify the large values of receding contact angles reported by Freer et al. (2002), we will continue to assume that hr ranges from 0j to 10j. Now we describe secondary imbibition in which water displaces NAPL. Due to aging, the mineralogy of the solid surfaces, and the chemical composition of the fluids, these surfaces can change their wettability, i.e., the receding contact angle in drainage can change to a larger advancing contact angle in imbibition (Buckley et al., 1995; Buckley and Liu, 1998; Freer et al., 2002; Hirasaki, 1991; Morrow et al., 1986). Because the advancing contact angles are greater than (or equal to) the receding contact angles, the NAPL/water interface remains pinned until the advancing contact angle is reached. Once this happens, the interface starts sliding. If the sum of the advancing contact angle, ha, and the corner half-angle, b, is less than 90j, the imbibition is spontaneous ( Pc>0); Fig. 1(b). If, on the other hand, this sum is greater than 90j, the imbibition is forced ( P V 0); Fig. 1(c). For very large advancing contact angles, we may create the intermediate NAPL layers near the pore corners as shown in Fig. 1(d). Further description of the two-fluid configurations during primary drainage and secondary imbibition processes is provided in the works of Al-Futaisi and Patzek (2003b), Øren et al. (1998) and Patzek (2001). In this paper, we use the mixed-wet displacement scenario described above for a single pore to study the effects of changing the advancing contact angles, the fraction of the NAPL-wet pores, the spatially inhomogeneous NAPL/water interfacial tension, and the initial water saturation. We report the macroscopic transport properties of two-phase flow, the displacement regime, the capillary pressure curve, the relative permeabilities, and the trapped NAPL saturation.4 Since an accurate procedure for quantifying the contact angles is yet to be provided, we believe that the best we can do at this moment is to assume ranges of uniformly random contact angles. We consider three different types of wetting: waterwet (advancing contact angles 20j to 55j), intermediate-wet (55j to 120j), and NAPLwet (120j to 155j). The advancing contact angles are drawn from a uniform probability distribution and correlated with the duct sizes (i.e., larger ducts are assigned larger contact angles). 4. Effects of advancing contact angles Al-Futaisi and Patzek (2003b) analyzed the effects of narrowly varying advancing contact angles on the two-phase flow characteristics. Here we compare the flow behavior in the three types of network wettability: water-wet (advancing contact angles 20j to 55j), intermediate-wet (55j to 120j), and NAPL-wet (120j to 155j). We assume that the receding contact angles during primary drainage are between 0j and 10j. We also assume that the NAPL/water interfacial tension, rN/w, is 35 mN/m; the initial water saturation in imbibition, Swi, is 6% (the maximum capillary pressure during primary drainage, Pmax c , is 4 In the subsequent discussion, we will be using the word ‘‘network’’ to represent a soil, rock, or any sediment. The parts of each pore, pore throats and pore body, will be replaced with the angular cylindrical ducts of small and large cross-sectional areas, respectively. A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 67 188 kPa); and the no-slip boundary condition at the NAPL/water interfaces. Fig. 2 shows that the three different wetting conditions result in different capillary pressures and relative permeabilities and, hence, in different two-phase flow behavior. 4.1. Water-wet In this wetting condition, secondary imbibition is spontaneous ( Pc>0). As described by Al-Futaisi and Patzek (2003b), this type of invasion begins inside the network by snap-off in the narrowest ducts (pore throats). When advancing contact angles are close to zero, snap-off results in high NAPL trapping. Here the advancing contact angles are large (20j to 55j), and the initial snap-offs are followed by the piston-like cooperative pore-body fillings that form growing compact clusters of water-filled ducts. The growth of compact water clusters reduces the NAPL trapping caused by snap-off. The trapped NAPL saturation for this wetting condition is 25%. This percent increases if the contact angles are less than 20j, and decreases if contact angles are between 55j and 90j. 4.2. Intermediate-wet Here, secondary imbibition is first spontaneous ( Pc>0), and then forced ( Pc < 0) if capillary pressure can be lowered sufficiently. The spontaneous imbibition occurs in ducts with advancing contact angles less than 90j (water-wet pores), whereas the forced imbibition occurs in ducts with advancing contact angles greater than 90j (NAPL-wet pores). As demonstrated by Al-Futaisi and Patzek (2003b), the range of contact angles considered in this wetting condition, 55j to 120j, results in a complex mixture of different displacement regimes. The contact angles between 55j and 90j are characterized by some snap-off and growth of compact water clusters that reduce the NAPL trapping. In contrast, the advancing contact angles between 90j and 100j favor piston-type invasion from the network inlet into the largest ducts, without creation of the intermediate NAPL layers near the duct corners, Fig. 1(c). The latter range of advancing contact angles results in strong NAPL trapping due to bypassing. Lastly, the contact angle range from 100j to 120j results in piston-type invasion from the network inlet and creation of the intermediate NAPL layers, Fig. 1(d). These layers enhance NAPL connectivity in the network and reduce the NAPL trapping. With these different flow regimes in mixed-wet networks, the ratio of NAPL-wet ducts and waterwet ducts has a dramatic effect on two-phase flow. The trapped NAPL saturation in the mixed-wet case is about 36%. 4.3. Oil-wet For this wetting condition, secondary imbibition is entirely forced piston-type displacement ( Pc < 0). Since advancing contact angles are now very large, it is easy to create the stable intermediate NAPL layers near most of the duct corners. These numerous layers are well connected, and trapping the NAPL decreases. The trapped NAPL saturation is about 7%. Smaller trapped NAPL saturation could be reached if larger contact angles were 68 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 69 used (e.g., 160j to 180j). However, we should emphasize that the connectivity of the intermediate NAPL layers is complex and not yet fully modeled. We probably overestimate the layer connectivity from one duct to another by assuming that the layers are connected as long as at least one layer exists in each pair of joined ducts. Notice that the shape of the capillary pressure curve in this case is similar to that obtained in primary drainage when NAPL migrates into the water-filled network. With all these displacement regimes, it becomes clear why the respective relative permeabilities are so different for the three wetting conditions; Fig. 2(b) and (c). In the NAPL-wet condition, one observes that the water relative permeability is the highest and the NAPL relative permeability is the lowest. In this wetting condition, NAPL moves in the thin intermediate layers, whereas water moves along the corners and the centers of the ducts (cf. Fig. 1(d)). The lowest water relative permeability is observed for the intermediate-wet condition, because water remains pinned near the duct corners without invading the duct centers. The NAPL relative permeability in the latter case is at first similar to that in the water-wet condition, but then it becomes lower because of significant NAPL trapping. For the water-wet condition, the water relative permeability is between those in the intermediate-wet and NAPL-wet conditions, while the NAPL relative permeability is the highest because the NAPL flows predominantly in the duct centers. One also observes that close to the trapped saturation, the NAPL relative permeability curve has a positive slope for the waterwet condition and close to zero slope for the other two conditions. 5. Effects of the fraction of NAPL-wet pores In this section, we analyze secondary imbibition in the intermediate-wet network. Because this type of network contains both water-wet and NAPL-wet ducts, the ratio of the NAPL-wet ducts to the water-wet ducts is important. We therefore vary this fraction to study its effect on the flow of water and NAPL. We assign to the water-wet and the NAPL-wet ducts advancing contact angles from 55j to 90j and 90j to 120j, respectively. An array of one random advancing contact angle per duct in the network is generated from a uniform probability distribution. Then, for each duct, a contact angle is drawn from this array with the magnitude proportional to the radius of a circle inscribed in the duct cross-section, i.e., the largest ducts are assigned the largest advancing contact angles and the smallest ducts are assigned the smallest contact angles. The fraction of the NAPL-wet ducts, f, is defined as the ratio of the number of NAPL-wet ducts to the total number of ducts in the network (Heiba et al., 1983) ( f = 0 means that the entire network is water-wet, ha = 55– 90j, whereas f = 1 means that the network is entirely NAPL-wet, ha = 90 – 120j). Again, we assume hr = 0j to 10j, rN/w = 35 mN/m, Swi = 6%, Pmax = 188 kPa, and the no-slip NAPL/water interface boundary c condition. Fig. 2. Secondary imbibition capillary pressures and relative permeabilities for the three wetting conditions: water-wet, intermediately wet, and NAPL-wet. 70 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 71 Fig. 4. Effects of the interfacial tension on the secondary imbibition capillary pressures and relative permeabilities in water-wet network. Fig. 3(a) –(c) shows the capillary pressures and relative permeabilities as functions of the fraction of NAPL-wet ducts. Small changes in the fraction of NAPL-wet ducts result in dramatic changes of flow characteristics of the network. Except for the cases f = 0 and f = 1, the capillary pressure curves in Fig. 3(a) are composed of the spontaneous imbibition part and the forced imbibition part. For f = 0, the displacement is entirely spontaneous, whereas for f = 1 it is entirely forced. As f increases, the forced imbibition part of the capillary pressure curve grows and the spontaneous imbibition part shrinks. The trapped NAPL saturation, Fig. 3(a), increases as we increase the fraction of NAPL-wet ducts up to some critical value between 0.4 and 0.5, after which the trapped NAPL saturation starts to Fig. 3. Effects of the fraction of NAPL-wet ducts on the secondary imbibition capillary pressures and relative permeabilities. 72 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 decrease. The increase of the trapped NAPL saturation is due to the introduction of some NAPL-wet ducts in which the intermediate NAPL layers cannot exist and, thus, NAPL bypassing increases. On the other hand, the decrease in the trapped NAPL saturation is due to the existence of the NAPL-wet ducts that allow the creation of continuous, stable intermediate NAPL-layers near the duct corners. The fraction of NAPL-wet ducts has great impact on the NAPL and water relative permeabilities; see Fig. 3(c). In general, the water relative permeability decreases as we increase f up to 0.4. Above f = 0.4, the water relative permeability increases for water saturations less than 0.5 and decreases for the saturations greater than 0.5. The NAPL relative permeability, in general, decreases as the fraction of NAPL-wet ducts in the network increases. However, the NAPL relative permeability Fig. 5. Effects of the interfacial tension on the secondary imbibition capillary pressures and relative permeabilities in intermediate-wet network. A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 73 increases for f between 0.8 and 1.0. The calculated significant dependance of the relative permeability functions on the fraction of NAPL-wet ducts raises questions about the validity of the relative permeability curves used in the field-scale simulators. 6. Effects of NAPL/water interfacial tension In the previous sections, row was spatially uniform and equal to 35 mN/m. Here, we fix the network wettability property and vary the NAPL/water interfacial tension, rN/w. We perform secondary imbibition displacements on the water-wet, intermediately wet, and Fig. 6. Effects of the interfacial tension on the secondary imbibition capillary pressures and relative permeabilities in NAPL-wet network. 74 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 Fig. 7. The secondary imbibition capillary pressure and relative permeability curves for the variable interfacial tension between 15 and 75 mN/m (dotted lines), and the constant value of 45 mN/m (solid lines). NAPL-wet networks using seven different values of rN/w: 15, 25, 35,45, 55, 65, 75 mN/m. These values are assumed to be constant in the network during each simulation. The capillary pressure and relative permeability curves for each wetting condition are plotted in Fig. 4 for the water-wet, Fig. 5 for intermediate-wet, and Fig. 6 for NAPL-wet case. Because in the calculation of the capillary entry pressures, rN/w is a common factor (see Al-Futaisi and Patzek, 2003b), a new value of rN/w will simply rescale the single dimensionless capillary pressure curve for primary drainage and secondary imbibition, e.g., the capillary pressure curve for rN/w = 55 mN/m can be obtained by multiplying the Fig. 8. Influence of the initial water saturation on the secondary imbibition capillary pressure and water and NAPL relative permeabilities in water-wet network. A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 75 76 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 35 mN/m capillary pressure curve by 55 = 35. The tiny differences in the trapped NAPL saturation and the relative permeabilities to water NAPL are caused by the roundoff error in the simulator. Now, let us use a range of rN/w values spatially distributed in the network. Fig. 7(a) compares the secondary imbibition capillary pressure curves for the three types of wet ting using constant rN/w = 45 mN/m (solid lines) and the spatially random rN/w between 15 and 75 mN/m (dotted lines). The primary drainage and the NAPL-wet secondary imbibition capillary pressure curves show more variability than the corresponding ones for the water-wet and intermediate-wet conditions. However, practically, these differences are negligible. Notice that in the water-wet and intermediate-wet conditions there is a slight difference in the trapped NAPL saturation. Fig. 7(b) plots the secondary imbibition relative permeabilities for water and NAPL using constant rN/w = 45 mN/m (solid lines) and variable rN/w between 15 and 75 mN/m (dotted lines). There is a slight difference in the two curves. In general, except for the NAPL relative permeability in the intermediatewet condition, the constant rN/w resulted in a slightly higher water and NAPL permeabilities than those obtained using the constant rN/w. Again, this difference is small. 7. Effects of initial water saturation The maximum capillary pressure during primary drainage, Pmax c , establishes the initial condition (the initial water saturation and interface configurations) for the secondary imbibition. In this section, we study the effect of Pmax on the secondary imbibition flow c characteristics. We vary Swi for the three wetting conditions considered in present analysis: water-wet (contact angles 20j to 55j), intermediate-wet (55j to 120j), and NAPL-wet (120j to 155j). We assume hr = 0j to 10j, rN/w = 35 mN/m, and the no-slip NAPL/water interface boundary condition. The secondary imbibition displacements are performed with the initial water saturations, Swi = 6%, 7%, 10%, 13%, 18%, 24% and 38%. The maximum primary drainage capillary pressures that correspond to these saturations are, Pmax = 188, 20, c 10, 8, 6, 5 and 4 kPa, respectively. Figs. 8– 10 plot the secondary imbibition capillary pressures and relative permeabilities in the water-wet, NAPL-wet, and NAPL-wet networks, respectively. The results show strong effects of initial water saturation on the capillary pressure and the relative permeability curves. The respective capillary pressure curves are simply rescaled and shrunk. For water-wet and intermediate-wet networks, the trapped NAPL saturation does not experience large changes as Swi increases ( F 5%). However, in the NAPL-wet network, the trapped NAPL saturation increases noticeably with the increasing Swi. In waterwet networks, both water and NAPL relative permeabilities are slightly affected by the different initial water saturations. However, introducing some NAPL-wetness into the network results in a tremendous variation in the NAPL and water relative permeabilities. Fig. 9. Effects of initial water saturation on secondary imbibition capillary pressures and water and NAPL relative permeabilities in intermediate-wet network. A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 77 78 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 A. Al-Futaisi, T.W. Patzek / Journal of Contaminant Hydrology 74 (2004) 61–81 79 In the intermediate-wet network, as Swi increases, the NAPL and water relative permeabilities increase. The increase in the water relative permeability is more dramatic than in the NAPL one. The behavior of the NAPL-wet network is somewhat different. The effect of Swi is dramatic for both NAPL and water relative permeabilities. As the Swi increases, the water and NAPL relative permeabilities increase for the average water saturation below 0.5, and decrease for the average water saturation above 0.5. 8. Conclusions Our full quasi-static physics pore network model was used to study the effect of advancing contact angle, fraction of the NAPL-wet pores, interfacial tension, and initial water saturation on the secondary imbibition capillary pressures and relative permeabilities. We have used a single network geometry and connectivity, but with three different levels of mixed-wetting: water-wet (contact angles 20j to 55j), intermediate-wet (55j to 120j), and NAPL-wet (120j to 155j). For water-wet condition and with a reasonably high capillary pressure after the initial drainage, the spontaneous secondary imbibition begins in the volume of the sediment by snap-off. The initial snap-off events are followed by the piston-like cooperative pore-body fillings that form growing compact water clusters. For the intermediate-wet condition, the flow is a mixture of spontaneous and forced secondary imbibition processes. Snap-off and growth of compact water clusters reduce NAPL trapping. Invasion from the sediment’s boundary into the largest pores without creation of the intermediate NAPL layers near the pore corners increases NAPL trapping. Finally, piston-type invasion from the sediment’s boundary that creates intermediate NAPL layers reduces trapping. For the NAPL-wet condition, secondary imbibition is forced piston-type displacement that creates stable intermediate NAPL layers near most of the pore corners in the sediment. This wetting condition results in least NAPL trapping. The fraction of the NAPL-wet pores strongly influences two-phase flow in the sediment. The trapped NAPL saturation increases as the fraction of the NAPL-wet pores increases up to some critical value around 0:5, after which the trapped NAPL saturation starts to decrease. A wide range of possible shapes of the water and NAPL relative permeabilities is observed. Spatially variable interfacial tension between 15 and 75 mN/m has negligible effect on the flow characteristics. The initial water saturation, Swi, has some effect on the two-phase flow characteristics of water-wet sediments. With more NAPL-wet pores in the sediment, Swi starts to have a strong effect on the water and NAPL relative permeabilities. In intermediate-wet sediments, increasing Swi increases the NAPL and water relative permeabilities. The increase of the water relative permeabilities is more dramatic. In Fig. 10. Effects of initial water saturation on secondary imbibition capillary pressures and water and NAPL relative permeabilities in NAPL-wet network. 80 A. Al-Futaisi, T.W. 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