Abstract
This study examined the influence of preferential flow on pore water flows and marine nitrogen transport reaction in variable saturation and variable density coastal aquifers. The 2-D unconfined aquifer model established was based on the software COMSOL by coupling the dynamic and chemical processes together. The results showed that preferential flow affects groundwater flow and salinity distribution, leading to a more complicated mixing process. The preferential flow resulted in an increase in mixing zone area and the upper saline plume area of 10.33 and 2.62 m2, respectively, a decrease in saltwater wedge area of 7.22 m2, and an increase in nitrate (NO3-) removal efficiency from 7.9% to 8.97%. The NO3- removal efficiency increases progressively with the depth (h) and quantity (n) of preferential flows; however, it decreases after a certain quantity. Further quantitative analysis revealed an increase in the intensity of nitrification and dissolved oxygen inflow flux with preferential flow depth and quantity increase. This phenomenon usually occurs on coasts where biological caves are abundant. The results also offer significant implications for designing engineering measures to mitigate saltwater intrusion and are significant to prevent groundwater quality deterioration in coastal zones.
1 Introduction
Groundwater is an important freshwater resource for industrial and agricultural purposes in coastal areas (; ). Nitrate pollution has deteriorated the quality of groundwater around the world due to an increase in human population and urban development (; ; ). Saltwater intrusion (SWI), as a global problem, seriously threatens freshwater resources and coastal productivity (, ; , , ; , ). The NO3- concentration in drinking water derived from groundwater exceeds the standard permissible limit of 50 mg L-1 set by the World Health Organization (WHO) in most parts of the world (; ). In China, approximately 34.1% of groundwater resources are contaminated with NO3- (; ).
Groundwater flow and solute transport in aquifers under the tidal influence are very complex (Figure 1) (; , , ). Periodic tidal fluctuations can lead to the formation of two coexisting saltwater plumes in aquifers: (i) a saltwater wedge (SW) due to density-driven saltwater recirculation and (ii) an upper saline plume (USP) due to tide-driven saltwater recirculation (; ). Land-derived groundwater is generally transported between the SW and USP and discharged into the ocean near the low tide mark, which is an area where saltwater and freshwater mix between two different saltwater plumes. Several surveys have also reported a large number of macro-pores (such as crab burrows and invertebrate nests) in aquifers (; ; ; ; ) and found that macro-pores are mainly concentrated in the upper supratidal zone and intertidal zone (). The presence of crab holes and macro-pores increases the overall surface infiltration rate to a range of 0.1 to 1 m d-1, which is one to two orders of magnitude higher than the matrix hydraulic conductivity (). They are well recognized to act as preferential flow paths and enhance the infiltration rate of surface water (), impact the distribution of salinity (; ; ), and change solute transport by increasing the connectivity of otherwise impermeable muddy soils (; ), thus affecting biogeochemical processes in salt marshes (; ; ). studied a 3-D model simulated in the marsh with a two-layer soil configuration at the Chongming Dongtan wetland. Their results suggested that preferential flow can act as drains for the surrounding soil during the falling tide, which increases water exchange between marsh soils and tidal creeks. constructed a model, and the results of their analysis suggested that preferential flow can promote soil permeability and facilitate solute transport in salt marshes. Additionally, preferential flow increases the connectivity between the soil surface and groundwater (). It also intensifies the heterogeneity of the aquifer, leading to greater hydraulic conductivity (). Although demonstrated that large pores increase USP and reduce SW, the mechanism is unclear. All combined, these studies confirmed that preferential flow or tidal-induced complex pore water flow and preferential flow have significant influences on solute transport. However, the effects of preferential flow distributed in the tidal zone on groundwater flow and solute transport in coastal unconfined aquifers under tidal conditions are not clear.
Figure 1
Saltwater transports a large quantity of dissolved oxygen (DO), NO3-, ammonium ion (NH4+), and dissolved organic carbon (DOC) into the aquifer. Several chemical reactions such as DOC degradation, aerobic respiration, nitrification (NH4+ transformation to NO3-), and denitrification (NO3- transformation to N2) can take place (; ). These processes are affected by tidal force, which can change the recycling rate and chemical composition of saltwater (; ; ). established a 2-D estuarine subsurface flow model based on the numerical model, assuming that DO, NO3-, NH4+, and DOC primarily originate from rivers. Nitrification occurs in the shallow layers, while denitrification occurs in the deeper anaerobic layers. These reactions, which are both controlled by redox conditions and DOC concentrations, play an important role in determining NO3- in the aquifer. Preferential flow can affect nitrification and denitrification reactions by directly or indirectly changing soil properties (). These reactions are also influenced by the redox conditions, aeration, and particle composition of the solution (). conducted field observations and flow modeling to assess how crab burrows drive carbon exchange in an intertidal marsh in South Carolina. They found that the concentrations of dissolved inorganic and organic carbon in crab burrow pore water differ from that in the surrounding soil matrix, and the gas-phase concentrations of CO2 in crab burrows were approximately six times greater than that in ambient air. These results suggested that crab burrows increase the reaction of carbon. evaluated the effect of deep whale burial on NO3- removal efficiencies in aquifers and found that organic carbon sources affected NO3- removal since DOC not only provided the reactant for denitrification but also provided an anaerobic environment (DOC oxidation). investigated the effect of preferential flows on nitrification and denitrification in aquifers, and the results showed that preferential flows promoted sediment nitrification, and the degree of promotion was significant with the increase of density. conducted laboratory experiments and found that crab burrows significantly affected the concentrations of NH4+ and NO3- and significantly promoted the nitrogen exchange flux at the sediment–water interface. It can be seen that the preferential flow not only effectively changes the pore water flow and solute transport rate but also increases the oxygen content of the aquifer and the contact area between the sediment and O2, thus interfering with the reaction of NO3-.
So far, the effects of preferential flow distributed in the tidal zone under tidal conditions on pore water flow and nitrogen–sea source transport reaction in coastal unconfined aquifers remain unclear. In this study, numerical simulations were conducted to address the effects of preferential flow number and depth on the pore water flow, nitrification, and denitrification in sea sources under tidal action. The results might provide a theoretical reference for designing engineering measures to mitigate saltwater intrusion, groundwater quality management, and the ecological restoration of coastal zones.
2 Methods
The groundwater flow and solute transport reaction models are used to study the influence of preferential flow on salinity change, pore water flow, and nitrogen transport reaction in aquifers.
2.1 Groundwater flow and solute transport model
A 2-D coastal wetland model was developed to study the salinity change and solute transport of aquifers with variable saturation and density using the COMSOL finite element software. The simulation of flow with variable saturation and density was based on Richard’s equation (Equation 1). Solute transport was based on the advection–dispersion–reaction equation (Equation 2) in porous media ():
where ρ is fluid density (kg m-3), Ci is the concentration of species i (mM), P is the pressure (Pa), and Z is the elevation head (m). The value of ks is the saturated hydraulic permeability (Equation 3), while kr stands for the relative permeability (m s-1) (Equation 4), u is the Darcy velocity (m s-1), θ is the water content (-) (Equation 6), g is the acceleration of gravity (9.81m s-2), Qm in this equation represents a stress source term (kg m-3 s-1), wm is the specific moisture capacity (m-1) (Equation 5), D is the hydrodynamic dispersion coefficient (m2 s-1), Ri is the reaction rate for species i (mM s-1), Se is the effective saturation (-) (Equations 7, 8), and S is water storage (Pa-1). The constitutive relationship between relative permeability and pore pressure obeys the van Genuchten model ():
where θs and θr is the saturated water content and relative water content (-), respectively. K is the hydraulic conductivity (m s-1), where ni, which is related to m in Equation 8, and a is the fitting parameter which describes the shape of both the moisture (m-1) and relative permeability functions (-) obtained by van Genuchten ().
The model is a 2-D beach aquifer cross-section (Figure 1), where the left and bottom boundary (BAE) and the upper boundary (CD) are both set as no flow and zero solute flux boundaries (; ). The right boundary (DE) is set as the inland boundary, while the ocean boundary (BC) is the permeable layer that is used to represent the interface between the beach surface and seawater or atmosphere and assigned a semi-pervious layer or seepage face boundary. The process is realized by the following formula (Equations 9–11):
where Rb is the conductance term (s-1), defined as the ratio of the saturated hydraulic conductivity (ks) with a coupling length scale (L, m). It was set at a high value allowing water to readily move in and out of the interface. Hb is the external head representing sea level (m), H is the total head (m), and Csea is seawater salinity (ppt).
In order to deal with the boundary conditions reasonably, two conditions have been considered. When the aquifer is saturated and the external head (Hb) of the sea level is higher than the elevation head, the head difference is determined by the difference between the overlying seawater and the beach interface. However, if the total head (H) is higher than the sea level (Hb), and the pressure head is equal to or higher than the atmospheric pressure. The boundary is a seepage surface. If the value of Rb is 0 when the aquifer is unsaturated, the boundary is a no-flow boundary. The salinity is determined by the groundwater velocity at the node. If the velocity is inward (to the aquifer), the salinity is estimated by seawater salinity (Csea = 35 ppt). If the groundwater flows from an aquifer, the zero concentration gradient was specified at the nodes. Previous studies have demonstrated that this modeling approach is useful in describing the water level movement and residence times within the transition zone (; ).
A time-varying head (H(t)) Equation 12 was implemented at selected cells in this zone by:
where H(t) is tidal head (m), determined by time; Hmsl is the mean sea level (10 m); A is tidal amplitude (0.5 m); is the angular frequency; and T is the tidal cycle (semi-diurnal tide, 12 h). These parameters were used in many studies (; ).
The model domain represented a homogeneous and isotropic coastal aquifer with a thickness of 12 m and a sloping beach boundary (slope of 0.1; Figure 1), which was comparable to a typical sandy coastal aquifer system () with a hydraulic conductivity of 15 m d-1, longitudinal dispersion coefficient (aL) of 0.2 m, transverse dispersion coefficient (aT) of 0.02 m (), and porosity of 0.45. Moreover, seawater salt concentration and density were set to 35 ppt (mass fraction) and 1,025 kg m-3, respectively. The freshwater salt concentration of 0 ppt and a density of 1,000 kg m-3 (see Table 1) were both adopted from and .
Table 1
| Model parameters | |||
|---|---|---|---|
| Parameter | Description | Value | Units |
| K | Hydraulic conductivity | 15a | m d-1 |
| θ | Porosity | 0.45 | – |
| Se | Residual saturation | 0.1a | – |
| αL | Transverse diffusion coefficient | 0.2a | M |
| αT | Longitudinal diffusion coefficient | 0.02a | M |
| C0 | Seawater concentration | 35b,c | kg m-3 |
| Cf | Freshwater concentration | 0b,c | kg m-3 |
| ρs | Seawater density | 1025b,c | kg m-3 |
| ρf | Freshwater density | 1000b,c | kg m-3 |
| RN | NO3- removal efficiency | – | % |
| Boundary condition | |||
| NO3- | NO3- boundary concentration | 0.25a | mM |
| NH4+ | NH4+ boundary concentration | 0.2a | mM |
| DO | DO boundary concentration | 0.2a | mM |
| DOC | DOC boundary concentration | 0.75a | mM |
| Kinetic parameter | |||
| Rate constant for oxidation of DOC | 3.0 × 10-9d | s-1 | |
| Rate constant for nitrification | 4.8 × 10-6 | mM-1 s-1 | |
| Limiting concentration of O2 | 0.008d | mM | |
| Limiting concentration of NO3- | 0.001d | mM | |
Model parameters, boundary condition, and kinetic parameter.
Units for solutes are in mmol dm-3 pore water, denoted as mM, background concentrations are set to 0.
a, ;
b, ;
c, ;
d, .
The preferential flow had a width of 0.16 m and was assumed to be a homogeneous medium with high permeability and porosity (the permeability was 100 times higher than that of the matrix and the porosity was set as 1). This technology enabled simulations of the preferential flow rapid responses to tidal-water-level fluctuations without affecting the simulation results (). Similar techniques and parameters have been used in groundwater models to simulate pore water flow and solute transport induced by macro-porosity (; ). The preferential flow was set upstream of the intertidal zone, and this was adopted from other studies where it was reported that preferential flow is mainly concentrated in the upper supratidal zone and intertidal zone (; ).
For all simulations, the mesh density increased in the preferential flow zones and at the beach. The values for the Courant number and numerical Péclet number did not exceed 1 and 4, respectively, which satisfied the stability criterion and avoided numerical oscillation. During the simulation, a constant temperature was maintained, resulting in constant dynamic viscosity.
The simulation first conducted a no-preferential flow model under the tidal action. Subsequently, to investigate the influence of depth and quantity of preferential flow, we set different depths (2.3, 3.3, and 4.3 m) and quantities (from 1 to 3) of preferential flow conditions under the tide action (five groups of experiments were conducted). The specific parameters are listed in Table 2.
Table 2
| Case | Tide | Depth (m) | Quantity (n) | TOE (m) | Average salinity (ppt) |
|---|---|---|---|---|---|
| Case1 N-P | √ | × | × | 24.20 | 7.21 |
| Case2 P-1 | √ | 2.30 | 1 | 23.10 | 7.19 |
| Case4 P-2 | √ | 3.30 | 1 | 23.09 | 7.03 |
| Case5 P-3 | √ | 4.30 | 1 | 22.90 | 7.00 |
| Case6 P-4 | √ | 4.30 | 2 | 22.35 | 6.96 |
| Case6 P-5 | √ | 4.30 | 3 | 22.50 | 6.94 |
Model parameters and TOE and average salinity.
2.2 Solute reaction model
To study the transformation of marine nutrients, a reaction network of four reactive species was applied to the reaction model. The model considered nitrification, denitrification, aerobic respiration, and DOC degradation.
The reaction model simulated the first-order reaction that required mixing for the inflow of DO, NO3-, NH4+, and DOC. The study omitted the production of NH4+ from DOC degradation and nitrification and only focused on the transformation of NO3- from marine-derived sources. The reactions and kinetic rate expressions are shown in Table 3. validated this reaction network by comparing the simulation results with field data from the Cape Shores beach adjacent to Delaware Bay.
Table 3
| Reaction | Rate expression | |
|---|---|---|
| DOC degradationa Aerobic respirationb Nitrificationb Denitrificationb | DOC→CO2 DOC+O2→CO2+H2O NH4++2O2 + 2HCO3-→NO3-+2CO2 + 3H2O 5DOC+4NO3-+4H+→5CO2 + 7H2O+2N2 | Rate= [DOC] If [O2] >; Rate = [DOC] If [O2]< ; Rate = [DOC] Rate = [NH4+][O2] If [O2] > ; Rate = 0 If [O2]< and [NO3-] > ; Rate = [DOC](1- ) If [O2]< and [NO3-]< ; Rate = [DOC](1- ) |
Reaction and kinetic rate expressions.
.
.
Based on the studies of and , the parameters of the reactions are shown in Table 1. This study determined the influence of preferential flow under tide influence on the chemical transformations in a nearshore aquifer. The sensitivity analyses on the specific kinetic parameter values adopted were not performed, although these parameter values vary in different coastal settings. Similar to salt transport, the nutrient concentration was set along with the aquifer–ocean interface for the reactive solutes. The boundary conditions of the nutrients are presented in Figure 1, and the specific nutrient values are shown in Table 1. The TOE (the saltwater wedge toe) was used to evaluate the length of the saltwater wedge, and the NO3- removal efficiency (RN) Equation 13 was quantified by:
where Ω is the domain area, t is the tidal cycle time (12 h), fb is the boundary flux, is the rate of NO3- reaction, and l is the length of the boundary layer.
We performed four steps: (i) groundwater flow and salinity distributions for all cases at the static water level were run to steady state, (ii) the hydraulic gradient and salinity distributions obtained at the static water level were used as the initial conditions under tidal action, (iii) the salinity distributions obtained in step (ii) were used as the initial conditions for the chemical solute transport and were run to steady state; (iv) and the results of the previous step were run as the initial conditions for the reaction network until they stabilized. The simulations were run for 700 days to allow the reactive solutes to reach equilibrium.
3 Results
3.1 Model calibration
To verify the reliability of the model, we developed a numerical model consistent with the lab experiment of , with an aquifer length of 4 m and width of 0.7 m and porosity of 0.45; the parameters a and ni were set to 5.9 m-1 and 2.68, respectively, and the longitudinal dispersion coefficient (aL) was 0.005 m and transverse dispersion coefficient (aT) was 0.0005 m [for the specific parameters, please refer to for details]. We consider three case conditions: non-preferential flow, preferential flow at x = 0.8 m, z = 0.3 m, and preferential flow at x = 1.8 m, z = 0.3 m, and the preferential flow scales and parameter settings are also consistent with those of .
From the experimental results in and numerical simulation results (Figure 2), the simulated results matched the experimental in all cases well (Figure 2). We can find that tidal forcing formed a USP and SW in the intertidal zone where saltwater infiltrated near the high tide mark and was discharged near the low tide mark. A fresh groundwater discharge zone (FDZ) separated the circulation cell from the lower interface located at the base of the beach. As expected, under the impact of preferential flow, when the preferential flow location is at x = 0.8 m, it has some effect on the salinity distribution and reduces the saltwater wedge deed extension. When the preferential flow location was at x =1.8 m, it has little effect on the salinity distribution, which is consistent with the salinity distribution pattern of the no-preferential flow condition.
Figure 2
The experimental and numerical results consistently demonstrated that the preferential flow could affect the salinity distribution in terrestrial environments, and the 2-D numerical model could be used to predict the water–salt exchange processes in aquifers.
3.2 Salinity and pore water flow
The salinity distribution under two different conditions is presented in Figure 3. Preferential flow modified the salinity distribution under tidal influence. The average salinity (average value of the whole aquifer) in the aquifer decreased from 7.21 to 7.03 ppt, while the TOE decreased from 24.2 to 23.09 m. Under the tidal condition (Figure 3), the area of the mixing zone (MZA) (the area between 10% and 90% salinity contour) was 53.87 m2, the area of USP (USPA) was 10.37 m2, and the area of SW (SWA) was 156.0 m2. However, under the preferential flow, the mixing zone and USP were increased, and SW was decreased, i.e., the MZA is 64.20 m2, the USPA is 12.98 m2, and the SWA is 148.79 m2. This indicated that the preferential flow enhanced freshwater–saltwater mixing and USP (Figure 3E); the preferential flow weakened the length of SW in the aquifer and reduced the salinity.
Figure 3

Simulation results: salinity distribution of tidal action in (A, B), the pink, black, and white solid lines show the 10%, 50%, and 90% salinity contour, respectively. Saltwater wedge (SW), upper salinity plume (USP), saltwater wedge toe (TOE), and fresh water discharge area (FDZ). TOE is the intersection of 50% salinity contour and x-axis. The horizontal black dotted line shows the average sea level and tidal range. In (C, D), the white solid line and data are particle path and travel time (unit: day). The particles start from the inland boundary and the beach, respectively. The gray vertical line indicates the preferential flow (h = 3.3 m). (E) Salinity difference graph (preferential flow - no preferential flow).
To determine the effect of preferential flow on groundwater flow, saltwater circulation, and saltwater–freshwater exchange under tidal conditions, the travel time for specified particles in the aquifer was calculated [readers may refer to
Table 4
| Starting position (m) | No preferential Flow (d) | h = 2.3 m (d) | h = 3.3 m (d) | h = 4.3 m (d) | n = 2 (d) | n = 3 (d) |
|---|---|---|---|---|---|---|
| x = 3 m, z = 7.42 m x = 8 m, z = 8.14 m x = 13 m, z = 8.8 m x = 75 m, z = 3 m x = 75 m, z = 6 m x = 75 m, z = 9 m | 1,026.9 465.9 176.7 267.8 259.7 257.1 | 1,007.6 453.1 181.6 273 265.4 258.1 | 908.4 404.5 172.2 276.7 272 258.2 | 927.1 406.9 183 280.6 269.6 258.4 | 851.2 375.8 161.1 283.7 268.9 259.4 | 872.2 395.7 165.4 281.5 269.4 257.5 |
Particle travel times and starting position.
Under tidal action (Figure 3), a USP developed in the intertidal zone, with particles released from inland along the moving path of freshwater bypassing the USP and SW discharge to the sea. The deeper particles took longer than those in the shallow, e.g., the one starting from the shallow (x = 75 m, z = 9 m) took 257.1 d, while that from the deep inland (x = 75 m, z = 3 m) took 267.8 d (Figure 3), increasing by 4.2%. The difference in travel time among the three particles at the seaside varied dramatically as the particles released to the deeper beach moved further landward and took longer paths, e.g., the particle starting from x = 13 m, z = 8.8 m took 176.7 d, while that from x = 3 m, z = 7.42 m took 1,026.9 d (Figure 3, Table 4).
Preferential flow leads to pore water flow and an increase in USP. Therefore, the particles released from the inland shallow layer experienced USP resistance across the preferential flow, with the travel time increased slightly, e.g., it took 257.1 d for particles released from x = 75 m and z = 9 m and 258.2 d for preferential flow (Figure 3). The travel time of particles released from the beach was consistent with the travel time under non-preferential flow, decreasing with an increase in USP, e.g., the particle released from x = 3 m and z = 7.42 m needed 1,026.9 d with the non-preferential flow but only 908.4 d in the presence of preferential flow.
To further discuss the influence of preferential flow on groundwater flow and circulation, Figure 4 presents the velocity distribution of rising tide, high tide, falling tide, and low tide without and with preferential flow. Only the velocity distribution in the area of preferential flow is shown for comparison. As shown in Figure 4, the velocity distribution differed with the seawater level. When the tide rose, salt water flowed into the aquifer through the intersection of the tidal level and the aquifer. When the tide fell, the tidal water retreated, and the pore water flowed to the ocean (Figure 4). Under the preferential flow condition at the rising tide, a relatively large pore water velocity appeared and rapidly flowed into the aquifer, thereby providing a preferential gateway for the pore water. When the flood completely flowed over the marsh platform (t = 3 h), the saltwater level reached the maximum (10.5 m), and a sharp rise in the pore water velocity near the preferential flow model was observed [Figure 4—(2B)]. The direction of the pore water flow under preferential flow was vertically downward, and the magnitude increased considerably. This indicated that the over-topping water rapidly enters preferential flow and diffuses into the surrounding marsh soil. Furthermore, preferential flow enhances the mixing and dilution of saltwater–freshwater, thus reducing the salinity of groundwater and increasing the quality of drinking water.
Figure 4

Simulation results: flow velocity at rising tide (t = 1 h), high tide (t = 3 h), falling tide (t = 6 h), and low tide (t = 9 h), (1A) - (4A), (1B) - (4B) under without and with preferential flow, respectively. (Note: for comparison, only the velocity distribution in the area where the preferential flow).
3.3 Distribution of nutrients
The distributions of DO, NO3-, NH4+, and DOC under tidal [Figure 5—(1A), (2A), (3A), and (4A)] and preferential flow conditions [Figure 5—(1B), (2B), (3B), and (4B)] are presented in this section. There were differences in the distribution of nutrients. DO was mainly concentrated in the shallow layers of the aquifer and NO3- was in the shallow and medium layers of the aquifer (Note: we used shallow, middle, and deep zones to differentiate the characteristics of the distribution area of DO, NO3-, NH4+, and DOC. In this study, these three intervals are a relative region varying with the preferential flow, so we are only distinguishing between the same model) [Figure 5—(1A), (1B), (2A), and (2B)], while NH4+ [Figure 5—(3A) and (3B)] and DOC [Figure 5—(4A) and (4B)] were distributed in the entire aquifer with a relatively high concentration in the shallow layer and in the middle and shallow layers, respectively, e.g., the average concentration of DOC in the region z > 4 m is 0.058 mM larger than that at z< 4 m (0.025 mM), and the average concentration of NH4+ in the region z > 4 m is 0.012 mM larger than that at z< 4 m (0.011 mM). The nutrient concentration increased along preferential flow in the reaction process [Figure 5—(1B), (2B), (3B), and (4B)].
Figure 5

Simulation results: nutrient concentration distribution without preferential flow action (A) and with preferential flow action (B) (1), (2), (3), and (4) is DO, NO3-, NH4+, and DOC distribution after reaction, respectively. The black solid line is the isoline of denitrification, and the gray vertical line indicates the preferential flow; note that only the intertidal zone is shown.
3.4 Reaction rate distribution
The reaction rate distributions of nitrification [Figure 6—(1A) and (1B)], denitrification [Figure 6—(2A) and (2B)], respiration [Figure 6—(3A) and (3B)], and DOC degradation [Figure 6—(4A) and (4B)] are described in this section.
Figure 6

Simulation results: reaction distribution (mM s-1). (1C)–(4C) is nitrification, denitrification, aerobic respiration, and DOC degradation reaction zone comparison under tidal and preferential flow. The gray vertical line indicates the preferential flow, PF is preferential flow.
Nitrification and respiration occurred primarily in the surface layers of the aquifer, while denitrification was dominant under the influence of anaerobic bacteria in the middle and deep layers where oxygen is depleted (Figure 6). DOC degradation occurred in the USP and SW of the whole aquifer under tidal action and preferential flow. However, the reaction rate in the middle and upper layers was relatively high [Figure 6—(4A) and (4B)], e.g., the average rate of DOC degradation in the region z > 4 m is 1.49 × 10-5 mM d-1 larger than that at z< 4 m (6.54 × 10-6 mM d-1). Compared to the non-preferential flow condition, preferential flow resulted in the extension of nitrification, respiration, and DOC degradation along with the preferential flow in the reaction process. However, denitrification consistently took place in the deeper USP.
We quantitatively analyzed the NO3- removal efficiency (RN). Under non-preferential flow condition, the RN is 7.9%. When we insert the preferential flow, the NO3- removal efficiency (RN) was modified, e.g., under the preferential flow action, the RN is 8.97%. These results suggest that preferential flow increases the NO3- removal efficiency, thus decreasing the salinity distribution.
3.5 Sensitivity analysis
3.5.1 Preferential flow depth
The mixing zone and USP increased vertically with preferential flow depth, the retreat of SW, and the decrease in salinity in the aquifer with an increase in preferential flow depth (Figure 7), e.g., when the preferential flow depth was 2.3 m, MZA was 59.04 m2, USP was 12.50 m2, SW was 152.50 m2, salinity was 7.19 ppt, and TOE was 23.10 m, and when the preferential flow depth was increased to 4.3 m, MZA was 69.11 m2, USP was 13.01 m2, SW was 147.22 m2, salinity was 7.00 ppt, and TOE was 22.90 m (Figure 7).
Figure 7

Simulation results: the mixing zone area (MZA) (A), the USP area (USPA) (B), the SW area (SWA) (C), the salinity (D), TOE (E), and the NO3- removal rate (RN) (F) with a different preferential flow depth.
The travel time of particles released from deep inland increased with preferential flow depth. With the persistent vertical increase of USP, the travel time and path of the particle passing the USP became longer, e.g., the particle released from x = 75 m and z = 3 m took 273 d and 280.6 d with depth that was 2.3 and 4.3 m, respectively. The travel time of the particle released from the beach was consistent with the previous section, decreasing with the preferential flow depth, e.g., the particle released from x = 3 m and z = 7.42 m took 1,007.6 d with depth that was 2.3 m, while under the preferential flow with depth at 4.3 m, it only required 927.1 d. This might be due to the retreat of SW with the change in preferential flow depth (Figure 8, Table 4).
Figure 8

(A–C) Simulation results: rate of change in particle transport time. Positive values indicate an increase, while negative values indicate a decrease, and the colors and the data in parentheses are the coordinates of the particle release point.
The distribution of nutrients was consistent with the discussions in Sections 3.4 (Supplementary Figure S1). The significance of preferential flow depth on the distribution of nitrification, denitrification, respiration, and DOC degradation is shown in Supplementary Figure S2. All reactions were consistent with the discussions in Section 3.5. Nitrification and respiration consumption of deeper DO have their long residence time in the aquifer. Nitrification and respiration primarily occurred in the surface layers (Supplementary Figure S2). Denitrification was dominant in the middle and deep layers of the aquifer (Supplementary Figure S2), and DOC degradation occurred throughout the aquifer with a faster reaction rate in the middle and upper layers (Supplementary Figure S2). However, each reaction at the USP acted differently with preferential flow depth due to the rapid inflow of nutrients through the preferential flow, e.g., when the preferential flow depth was 2.3 m, the NO3- produced by nitrification was 3.184 g d-1, and the NO3- removal efficiency was 8.72%. However, under a preferential flow depth of 4.3 m, the NO3- produced by nitrification was 3.298 g d-1, and the NO3- removal efficiency was 9.04%.
3.5.2 Preferential flow quantity
The USP increased with preferential flow quantity, MZ increases and then decreases, SW decreases and then increases and decrease in salinity in the aquifer with an increase in preferential flow quantity (Figure 9), e.g., when the preferential flow was 1, MZA was 69.11 m2, USP was 13.01 m2, SW was 147.22 m2, salinity was 7.00 ppt, and TOE was 22.9 m, and when the preferential flow quantity was increased to 3, MZA was 66.40 m2, USP was 13.63 m2, SW was 145.04 m2, salinity was 6.94 ppt, and TOE was 22.50 m (Figure 9).
Figure 9

Simulation results: the mixing zone area (MZA) (A), the USP area (MZA) (B), the SW area (MZA) (C), the salinity (D), TOE (E), and the NO3- removal rate (F) with a different number (n) of preferential flow.
The travel time of particles released from deep inland increased with preferential flow quantity. With the persistent vertical increase of USP, the travel time and path of the particle passing the USP became longer, e.g., the particle released from x = 75 m and z = 3 m took 280.6 d and 281.5 d at n = 1 and n = 3, respectively. The travel time of the particle released from the beach was consistent with the previous section, decreasing with the preferential flow quantity, e.g., the particle released from x = 3 m and z = 7.42 m took 927.1 d with n that was 1, while under the preferential flow with n that was 3, it only required 872.2 d (Figure 10, Table 4).
Figure 10

(A, B) Simulation results: rate of change in particle transport time. Positive values indicate an increase, while negative values indicate a decrease. The colors and the data in parentheses are the coordinates of the particle release point.
The significance of preferential flow quantity on the distribution of nitrification, denitrification, respiration, and DOC degradation is shown in Supplementary Figure S3. Nitrification and respiration consumption of deeper DO have their long residence time in the aquifer. Nitrification and respiration primarily occurred in the surface layers (Supplementary Figures S3, S4), while denitrification was dominant in the middle and deep layers of the aquifer (Supplementary Figure S3), and DOC degradation occurred throughout the aquifer with a faster reaction rate in the middle and upper layers (Supplementary Figure S4). However, each reaction at the USP acted differently with preferential flow quantity due to the rapid inflow of nutrients through the preferential flow, e.g., when the preferential flow quantity was 1, the NO3- produced by nitrification was 3.298 g d-1, and the NO3- removal efficiency was 9.03%; when the preferential flow quantity was 2, the NO3- produced by nitrification was 3.347 g d-1, and the NO3- removal efficiency was 9.04%. However, under a preferential flow quantity that was 3, the NO3- produced by nitrification was 3.34 g d-1, and the NO3- removal efficiency was 8.73%.
4 Discussion
4.1 Implication of preferential flow on pore water flow
A USP promotes the retreat of SW under tidal action, which renders the SW closer to the ocean and limits saltwater intrusion. Preferential flow enhanced (Figure 3) this effect, driving SW further seaward, and this impact gradually increases with the depth of preferential flows (Figures 7, 9). These results are consistent with those of
4.2 Implication of preferential flow on nitrification and denitrification
The nutrients from the sea were initially input in the numerical model with the salinity simultaneously. Nitrification primarily occurred in the surface layer (Figure 6, Supplementary Figures S2, S4) since nitrification, respiration consumption of deeper DO, and denitrification were dominant in the middle and deep layers of the aquifer (Figure 6, Supplementary Figures S2, S4).
In the presence of tidal action, the distribution of nutrients in the aquifer formed a USP and a SW. The travel and residence times were longer in the deeper layers of the aquifer for nutrients, nitrification, and respiration consumption of deeper DO (Figure 5, Supplementary Figures S1, S3), creating anaerobic conditions for denitrification. Subsequently, the NO3- produced was used up during denitrification, resulting in the reduction of NO3- in the deep layer (Figure 5—(2B), NO3- distribution). Denitrification occurred in the deeper USP as nitrification in the upper USP not only provided the reactant for denitrification but also offered an anaerobic environment. The NO3- removal efficiency increased compared to that in non-preferential flow, and this effect increases progressively with the depth and number of preferential flows; however, it decreases after a certain quantity. It can be observed that the existence of macro-porosity (such as crab burrows and invertebrate nests) facilitates the removal of NO3- from sea sources. Some previous studies demonstrated that denitrification also increased with the size of the mixing zone (
In addition,
4.3 Knowledge gaps and research needs
This study elucidated the effect of preferential flow on salinity change and solute transformation under tidal conditions. It determined the importance of the depth and quantity of preferential flow, which guide the mitigation of saltwater intrusion and contaminant removal. However, the location and density (
5 Conclusions
This study examined the combined effect of preferential flow and tide on pore water flow and marine nitrogen transport reaction in coastal aquifers. The following conclusions might be drawn:
(1) Under tidal action, preferential flow increases the hydraulic conductivity of the aquifer and accelerates the pore water flow and solute transport. The preferential flow results in the vertical increase of the USP and further retreat of SW. In the presence of preferential flow, the NO3- removal efficiency is increased.
(2) Nitrification mainly occurs in the surface layer of the aquifer, while denitrification dominates the middle and deep layers. The nitrification effect increases with the increase in the depth and quantity of preferential flow, and the NO3- removal efficiency increases progressively with the depth and number of preferential flows; however, it decreases after a certain quantity.
Statements
Data availability statement
The original contributions presented in the study are included in the article/Supplementary Material. Further inquiries can be directed to the corresponding authors. The model calibration experimental data used to produce Figure 2, A1, B1 and C1 are compiled from
Author contributions
CG: Conceptualization, Investigation, Methodology, Writing – original draft, Writing – review & editing. JK: Funding acquisition, Resources, Supervision, Visualization, Writing – review & editing. JW: Writing – review & editing. WC: Supervision, Writing – review & editing.
Funding
The author(s) declare financial support was received for the research, authorship, and/or publication of this article. This research was supported by the National Natural Science Foundation of China (51979095) and acknowledges the Postgraduate Research and Practice Innovation Program of Jiangsu Province (KYCX22_0658).
Conflict of interest
The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
Publisher’s note
All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.
Supplementary material
The Supplementary Material for this article can be found online at: https://www.frontiersin.org/articles/10.3389/fmars.2024.1369869/full#supplementary-material
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Summary
Keywords
preferential flow, marine nitrogen, nitrification, denitrification, removal efficiency
Citation
Gao C, Kong J, Wang J and Chen W (2024) Nitrate fate in coastal unconfined aquifers influenced by preferential flows. Front. Mar. Sci. 11:1369869. doi: 10.3389/fmars.2024.1369869
Received
13 January 2024
Accepted
04 March 2024
Published
11 April 2024
Volume
11 - 2024
Edited by
Tianyuan Zheng, Ocean University of China, China
Reviewed by
Yunhai Fang, Hefei University of Technology, China
Zhang Bo, Shandong University of Science and Technology, China
Qinpeng Chang, Ocean University of China, China
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© 2024 Gao, Kong, Wang and Chen.
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*Correspondence: Jun Kong, kongjun999@126.com; Jun Wang, junw1997@163.com
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